[seyf97]

Hi everyone!

I would like to model a condensing R22 vapor, and initially I started an example by modelling the User Defined Real Gas Model (UDRGM) given in the manual : https://www.afs.enea.it/project/nept...ug/node337.htm

I have compiled and built the code, but when I load it, I receive this warning message:

myGas.c

..\..\src\myGas.c(135): warning C4113: 'double (*)(double,double,double *)' differs in parameter lists from 'double (*)(cxboolean,double,double,double *)'





If I ignore the message and Hybrid Initialize, I get a message indicating:

turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 6250 cells



Then, when I run the calculation,

# Divergence detected in AMG for temperature, protective actions enabled!

and the calculation stops.

When I change relaxation, I only achieve 5-10 iterations which diverge dramatically. When I checked the results in Post-Processing, I realized that the pressure values are unrealistic, and std. initialization by default tries to initialize pressure to 2.e-11 Pa



Additional background info:

I run fluent from VS 2019 Command Prompt and then load my .MSH file from dp0/FFF/mech in order to build the UDF properly.
The geometry is a simple 2D rectangle (10mm x 100mm)
BC's:

Inlet: mass flow (0.001 kg/s)
Outlet: pressure outlet (0 pa gauge)
Temperature is patched to 300K


Any help is appreciated. Thanks.

[seyf97]

SOLVED. The UDRGM provided in the link is outdated, the one in the ANSYS software user's guide is working flawlessly.