|
[Sponsors] | |||||
Invalid Cp error at a specific temperature in Fluent |
![]() |
|
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
|
|
|
#1 |
|
New Member
MB
Join Date: Sep 2022
Posts: 8
Rep Power: 5 ![]() |
Dears,
I am simulating a free jet CO2 through a micro-orifice. I have supercritical upstream conditions, and subcritical downstream conditions. I am using Peng Robinson real gas equation. Model works perfectly fine as long as the inlet temperature is >310 K. If I reduce the the inlet temperature to less than that, the model diverges and I get the error 'Invalid Cp (- xxxxx) at T= xxxx'. Note that I am starting from a converged solution at T=310 K, and slightly changing T to 308 K (for example). I understand that this is a pseudo-critical region where properties of CO2 vary abruptly. So my question is would someone kindly suggest how to deal with this issue in Fluent? Thank you, |
|
|
|
|
|
![]() |
| Thread Tools | Search this Thread |
| Display Modes | |
|
|
Similar Threads
|
||||
| Thread | Thread Starter | Forum | Replies | Last Post |
| Averaging over iterations for steady-state simulation | CFD student | Fluent UDF and Scheme Programming | 8 | September 22, 2022 04:39 |
| [snappyHexMesh] Invalid Normals for source face to target face while making AMI? | Sorabh | OpenFOAM Meshing & Mesh Conversion | 1 | August 3, 2021 07:35 |
| Evaporation condensation below saturation temperature in FLUENT | user321 | Fluent Multiphase | 1 | January 29, 2020 06:41 |
| Calculation of the Governing Equations | Mihail | CFX | 7 | September 7, 2014 07:27 |
| Two-Phase Buoyant Flow Issue | Miguel Baritto | CFX | 4 | August 31, 2006 13:02 |