|
[Sponsors] |
February 5, 2016, 03:04 |
NIST databased refrigerants
|
#1 |
New Member
Pradeep Gupta
Join Date: Jun 2015
Posts: 5
Rep Power: 10 |
REFPROP_error (203) from function: tprho (density)
[TPRHO error 203] vapor iteration has not converged for T = 300.00 K, P = 3.1680 MPa, rho (last guess) = 6.6230 mol/L, x (mol frac) = 1.00000 I am using R134a as refrigerant and got the this error, What does it mean and how can I sort it out? Pls suggest me///// |
|
February 26, 2016, 12:39 |
same problem
|
#2 |
New Member
Merwin
Join Date: Feb 2016
Posts: 1
Rep Power: 0 |
I also using r134a for an analysis...import r134a by activating the NIST real gas using some commands then at the end of solution intialization the same refprop error mentioned above is displaying...anyone suggest me a solution for this problem
|
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Real gas NIST model problem | jexposito | FLUENT | 18 | November 26, 2020 05:41 |
[REQUEST HELP] Fluent 15.0 using NIST real gas model | Reivax | FLUENT | 0 | June 16, 2015 11:00 |
NIST model in Ansys-Fluent | b.shuvayan | FLUENT | 1 | April 3, 2013 11:02 |
Fire simulation using FDS from NIST | Jens | Main CFD Forum | 1 | January 22, 2004 01:53 |
Nist Fire Dynamic Simulator | Miren | Main CFD Forum | 3 | October 3, 2002 03:32 |