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reactingTwoPhaseEulerFoam: New twoPhaseEulerFoam supporting mass-tran…

…sfer and reactions

Multi-species, mass-transfer and reaction support and multi-phase
structure provided by William Bainbridge.

Integration of the latest p-U and face-p_U algorithms with William's
multi-phase structure is not quite complete due to design
incompatibilities which needs further development.  However the
integration of the functionality is complete.

The results of the tutorials are not exactly the same for the
twoPhaseEulerFoam and reactingTwoPhaseEulerFoam solvers but are very
similar.  Further analysis in needed to ensure these differences are
physical or to resolve them; in the meantime the twoPhaseEulerFoam
solver will be maintained.
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Henry Weller
Henry Weller committed Jun 12, 2015
1 parent 6ba9208 commit 3ed90ae73d3bd5a1114614a8ee869a6c0dd1335d
Showing 575 changed files with 88,511 additions and 0 deletions.
@@ -0,0 +1,11 @@
#!/bin/sh
cd ${0%/*} || exit 1 # Run from this directory
set -x
wclean libso phaseSystems
wclean libso interfacialModels
wclean libso interfacialCompositionModels
wclean libso phaseCompressibleTurbulenceModels
wclean
# ----------------------------------------------------------------- end-of-file
@@ -0,0 +1,13 @@
#!/bin/sh
cd ${0%/*} || exit 1 # Run from this directory
set -x
wmakeLnInclude interfacialModels
wmakeLnInclude interfacialCompositionModels
wmake libso phaseSystems
wmake libso interfacialModels
wmake libso interfacialCompositionModels
wmake libso phaseCompressibleTurbulenceModels
wmake
# ----------------------------------------------------------------- end-of-file
@@ -0,0 +1,51 @@
/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | Copyright (C) 2011-2015 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
This file is part of OpenFOAM.
OpenFOAM is free software: you can redistribute it and/or modify it
under the terms of the GNU General Public License as published by
the Free Software Foundation, either version 3 of the License, or
(at your option) any later version.
OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
for more details.
You should have received a copy of the GNU General Public License
along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
Global
CourantNo
Description
Calculates and outputs the mean and maximum Courant Numbers.
\*---------------------------------------------------------------------------*/
scalar CoNum = 0.0;
scalar meanCoNum = 0.0;
if (mesh.nInternalFaces())
{
scalarField sumPhi
(
fvc::surfaceSum(mag(phi))().internalField()
);
CoNum = 0.5*gMax(sumPhi/mesh.V().field())*runTime.deltaTValue();
meanCoNum =
0.5*(gSum(sumPhi)/gSum(mesh.V().field()))*runTime.deltaTValue();
}
Info<< "Courant Number mean: " << meanCoNum
<< " max: " << CoNum << endl;
// ************************************************************************* //
@@ -0,0 +1,12 @@
#include "CourantNo.H"
{
scalar UrCoNum = 0.5*gMax
(
fvc::surfaceSum(mag(phi1 - phi2))().internalField()/mesh.V().field()
)*runTime.deltaTValue();
Info<< "Max Ur Courant Number = " << UrCoNum << endl;
CoNum = max(CoNum, UrCoNum);
}
@@ -0,0 +1,47 @@
{
autoPtr<phaseSystem::heatTransferTable>
heatTransferPtr(fluid.heatTransfer());
phaseSystem::heatTransferTable&
heatTransfer = heatTransferPtr();
{
tmp<fvScalarMatrix> he1Eqn(phase1.heEqn());
if (he1Eqn.valid())
{
he1Eqn =
(
he1Eqn
==
*heatTransfer[phase1.name()]
+ fvOptions(alpha1, rho1, phase1.thermo().he())
);
he1Eqn->relax();
fvOptions.constrain(he1Eqn());
he1Eqn->solve();
}
}
{
tmp<fvScalarMatrix> he2Eqn(phase2.heEqn());
if (he2Eqn.valid())
{
he2Eqn =
(
he2Eqn
==
*heatTransfer[phase2.name()]
+ fvOptions(alpha2, rho2, phase2.thermo().he())
);
he2Eqn->relax();
fvOptions.constrain(he2Eqn());
he2Eqn->solve();
}
}
}
fluid.correctThermo();
@@ -0,0 +1,3 @@
reactingTwoPhaseEulerFoam.C
EXE = $(FOAM_APPBIN)/reactingTwoPhaseEulerFoam
@@ -0,0 +1,24 @@
EXE_INC = \
-IphaseSystems/lnInclude \
-IinterfacialModels/lnInclude \
-IinterfacialCompositionModels/lnInclude \
-IphaseCompressibleTurbulenceModels/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/basic/lnInclude \
-I$(LIB_SRC)/transportModels/compressible/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/turbulenceModels/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/compressible/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/phaseCompressible/lnInclude \
-I$(LIB_SRC)/finiteVolume/lnInclude \
-I$(LIB_SRC)/fvOptions/lnInclude \
-I$(LIB_SRC)/meshTools/lnInclude \
-I$(LIB_SRC)/sampling/lnInclude
EXE_LIBS = \
-lreactingTwoPhaseSystem \
-lreactingEulerianInterfacialModels \
-lreactingEulerianInterfacialCompositionModels \
-lphaseReactingTurbulenceModels \
-lfiniteVolume \
-lfvOptions \
-lmeshTools \
-lsampling
@@ -0,0 +1,50 @@
{
autoPtr<phaseSystem::massTransferTable>
massTransferPtr(fluid.massTransfer());
phaseSystem::massTransferTable&
massTransfer(massTransferPtr());
PtrList<volScalarField>& Y1 = phase1.Y();
PtrList<volScalarField>& Y2 = phase2.Y();
forAll(Y1, i)
{
tmp<fvScalarMatrix> Y1iEqn(phase1.YiEqn(Y1[i]));
if (Y1iEqn.valid())
{
Y1iEqn =
(
Y1iEqn
==
*massTransfer[Y1[i].name()]
+ fvOptions(alpha1, rho1, Y1[i])
);
Y1iEqn->relax();
Y1iEqn->solve(mesh.solver("Yi"));
}
}
forAll(Y2, i)
{
tmp<fvScalarMatrix> Y2iEqn(phase2.YiEqn(Y2[i]));
if (Y2iEqn.valid())
{
Y2iEqn =
(
Y2iEqn
==
*massTransfer[Y2[i].name()]
+ fvOptions(alpha2, rho2, Y2[i])
);
Y2iEqn->relax();
Y2iEqn->solve(mesh.solver("Yi"));
}
}
fluid.massTransfer(); // updates interfacial mass flow rates
}
@@ -0,0 +1,7 @@
phase1.continuityError() =
fvc::ddt(alpha1, rho1) + fvc::div(alphaRhoPhi1)
- (fvOptions(alpha1, rho1)&rho1);
phase2.continuityError() =
fvc::ddt(alpha2, rho2) + fvc::div(alphaRhoPhi2)
- (fvOptions(alpha2, rho2)&rho2);
@@ -0,0 +1,73 @@
#include "readGravitationalAcceleration.H"
#include "readhRef.H"
Info<< "Creating phaseSystem\n" << endl;
autoPtr<twoPhaseSystem> fluidPtr
(
twoPhaseSystem::New(mesh)
);
twoPhaseSystem& fluid = fluidPtr();
phaseModel& phase1 = fluid.phase1();
phaseModel& phase2 = fluid.phase2();
volScalarField& alpha1 = phase1;
volScalarField& alpha2 = phase2;
volVectorField& U1 = phase1.U();
surfaceScalarField& phi1 = phase1.phi();
surfaceScalarField& alphaPhi1 = phase1.alphaPhi();
surfaceScalarField& alphaRhoPhi1 = phase1.alphaRhoPhi();
volVectorField& U2 = phase2.U();
surfaceScalarField& phi2 = phase2.phi();
surfaceScalarField& alphaPhi2 = phase2.alphaPhi();
surfaceScalarField& alphaRhoPhi2 = phase2.alphaRhoPhi();
surfaceScalarField& phi = fluid.phi();
dimensionedScalar pMin
(
"pMin",
dimPressure,
fluid.lookup("pMin")
);
#include "gh.H"
rhoThermo& thermo1 = phase1.thermo();
rhoThermo& thermo2 = phase2.thermo();
volScalarField& p = thermo1.p();
volScalarField& rho1 = thermo1.rho();
const volScalarField& psi1 = thermo1.psi();
volScalarField& rho2 = thermo2.rho();
const volScalarField& psi2 = thermo2.psi();
Info<< "Reading field p_rgh\n" << endl;
volScalarField p_rgh
(
IOobject
(
"p_rgh",
runTime.timeName(),
mesh,
IOobject::MUST_READ,
IOobject::AUTO_WRITE
),
mesh
);
label pRefCell = 0;
scalar pRefValue = 0.0;
setRefCell
(
p,
p_rgh,
pimple.dict(),
pRefCell,
pRefValue
);
@@ -0,0 +1,3 @@
IOMRFZoneList MRF(mesh);
MRF.correctBoundaryVelocity(U1);
MRF.correctBoundaryVelocity(U2);
@@ -0,0 +1,20 @@
massTransferModels/massTransferModel/massTransferModel.C
massTransferModels/massTransferModel/newMassTransferModel.C
massTransferModels/Frossling/Frossling.C
massTransferModels/sphericalMassTransfer/sphericalMassTransfer.C
surfaceTensionModels/surfaceTensionModel/surfaceTensionModel.C
surfaceTensionModels/surfaceTensionModel/newSurfaceTensionModel.C
surfaceTensionModels/constantSurfaceTensionCoefficient/constantSurfaceTensionCoefficient.C
interfaceCompositionModels/interfaceCompositionModel/interfaceCompositionModel.C
interfaceCompositionModels/interfaceCompositionModel/newInterfaceCompositionModel.C
interfaceCompositionModels/InterfaceCompositionModel/InterfaceCompositionModels.C
saturationPressureModels/saturationPressureModel/saturationPressureModel.C
saturationPressureModels/saturationPressureModel/newSaturationPressureModel.C
saturationPressureModels/Antoine/Antoine.C
saturationPressureModels/AntoineExtended/AntoineExtended.C
saturationPressureModels/ArdenBuck/ArdenBuck.C
LIB = $(FOAM_LIBBIN)/libreactingEulerianInterfacialCompositionModels
@@ -0,0 +1,27 @@
EXE_INC = \
-I../phaseSystems/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/specie/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/basic/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/reactionThermo/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/properties/liquidProperties/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/properties/liquidMixtureProperties/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/properties/solidProperties/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/properties/solidMixtureProperties/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/thermophysicalFunctions/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/reactionThermo/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/SLGThermo/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/chemistryModel/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/radiationModels/lnInclude \
-I$(LIB_SRC)/transportModels/incompressible/lnInclude \
-I$(LIB_SRC)/transportModels/compressible/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/turbulenceModels/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/compressible/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/phaseCompressible/lnInclude \
-I$(LIB_SRC)/finiteVolume/lnInclude \
-I$(LIB_SRC)/meshTools/lnInclude
LIB_LIBS = \
-lreactingTwoPhaseSystem \
-lfluidThermophysicalModels \
-lreactionThermophysicalModels \
-lspecie
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