 |
 |
 |
|
|
|
[Sponsors] | ||||
September 18, 2015, 18:35
|
Real gas NIST model problem
|
#1 |
|
New Member
Join Date: Jun 2014
Posts: 13
Rep Power: 11  |
Hello,
I am trying to run a simulation with real gas model from NIST using r134a as working fluid. When I try to initialisate or run the simulation I get the next message: Primitive Error at Node 0: REFPROP_error (203) from function: tprho (density) [TPRHO error 203] vapor iteration has not converged for T= 257.82 K, p =0.55582 MPA, rho (last guess) =0.39299 mol/L, x (mol frac) = 1.0000 I do not know how to make the Refprop function to converge. Anybody could give some advice about how to deal with it? Best regards. |
|
|
|
|
|
|
Similar Threads
|
||||
| Thread | Thread Starter | Forum | Replies | Last Post |
| Continuing User Defined Real Gas Model issues | aeroman | FLUENT | 6 | April 8, 2016 03:34 |
| Parallel User Defined Real Gas Model | aeroman | FLUENT | 4 | July 1, 2015 06:09 |
| How to model Liquid to Gas mass transfer (Stefan Problem) in Fluent? | hasib61 | Fluent Multiphase | 0 | December 24, 2014 17:24 |
| how to hook this udf | shanu | FLUENT | 1 | August 26, 2011 10:48 |
| Redlich Kwong real gas model for species mixture Helium and Argon | anandabbai | FLUENT | 0 | May 29, 2009 02:04 |
Threaded Mode
