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Inert compound that reacts #418
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The version I'm using is v8.3.4 for Windows. |
IMPORTANT: This section is for code-related bugs. For usage issues, please go to the Support Forums. |
@mjparra you can zip the simulation file and drag it here to attach. |
I already post my question in sourceforge, according to a suggestion I
received. But I attach the file here, this is a file that shows only the
part with the problem.
I appreciate ;your help.
Martha Parra
…On Thu, Jan 26, 2023 at 7:18 AM Daniel Wagner < ***@***.***> wrote:
@mjparra you can zip the simulation file and drag it here to attach.
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@mjparra <https://github.com/mjparra> you can zip the simulation file and
drag it here to attach.
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DanWBR
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Jan 26, 2023
When I check the third stream,that it must be zero, I found, that it appear
a very small negative number for mass flow, and -infinite for molar flow,
then it is impossible to calculate heat load:
Master Property Table
Object 16 15 14
Temperature 577 577 577 C
Pressure 204.75 204.75 204.75 kPa
Mass Flow -3.35E-16 1.51069 1.51069 kg/h
Molar Flow #¿NOMBRE? 0.157284 0.0852586 kmol/h
Volumetric Flow 0 1.51E-20 2.94432 m3/h
Molecular Weight (Mixture) 0 9.60482 17.7189 kg/kmol
Specific Enthalpy (Mixture) 0 0 1520.04 kJ/kg
Molar Flow (Mixture) / Nitrogen NaN 0.00035446 0.00062562 kmol/h
Molar Flow (Mixture) / Hydrogen NaN 0.105696 0 kmol/h
Molar Flow (Mixture) / Water NaN 0 0.019428 kmol/h
Molar Flow (Mixture) / Carbon monoxide NaN 0.0359574 0 kmol/h
Molar Flow (Mixture) / Carbon dioxide NaN 0.00079934 0.00141083 kmol/h
Molar Flow (Mixture) / Methane NaN 0.0135867 0.0598689 kmol/h
Molar Flow (Mixture) / Ethane NaN 0.00084879 0.00374016 kmol/h
Molar Flow (Mixture) / Propane NaN 4.20E-05 0.00018513 kmol/h
Energy Flow 0 -1493.59 -2153.09 W
Martha Parra
…On Thu, Jan 26, 2023 at 7:40 AM Martha Parra ***@***.***> wrote:
I already post my question in sourceforge, according to a suggestion I
received. But I attach the file here, this is a file that shows only the
part with the problem.
I appreciate ;your help.
Martha Parra
On Thu, Jan 26, 2023 at 7:18 AM Daniel Wagner <
***@***.***> wrote:
> @mjparra you can zip the simulation file and drag it here to attach.
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> receiving this because you were mentioned.Message ID:
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> @mjparra <https://github.com/mjparra> you can zip the simulation file
> and drag it here to attach.
>
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> unsubscribe
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I appreciate your dedication to solve the issue. When can we get an update
on this topic?
Thanks a lot,
Martha Parra
…On Thu, Jan 26, 2023 at 3:04 PM Daniel Wagner < ***@***.***> wrote:
@mjparra I've already fixed the issue, it was an error in the overall mass
balance. aac6d31 it will work in the next update/version. —Reply to this
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@mjparra <https://github.com/mjparra> I've already fixed the issue, it
was an error in the overall mass balance. aac6d31
<aac6d31>
it will work in the next update/version.
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IMPORTANT: This section is for code-related bugs. For usage issues, please go to the Support Forums.
Describe the bug
There is a conversion reactor (isothermic). One of the compounds is Nitrogen, it doesn't appear in any of the reactions, but in the outlet stream, Nitrogen is only 43% of the one that enter.
There is another issue: The heat load obtained is NaN, must it not be 0?
To Reproduce
Steps to reproduce the behavior:
Expected behavior
The amount of Nitrogen must be the same in the outlet stream.
The heat load must be zero, since is isothermic.
issueN2.pdf
Screenshots
![image](https://user-images.githubusercontent.com/123581700/214655691-457f423f-3802-4f1b-9f04-1f6458b2fa15.png)
If applicable, add screenshots to help explain your problem.
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Additional context
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