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#1 |
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Member
Prateek Anand
Join Date: Nov 2012
Posts: 34
Rep Power: 15 ![]() |
Hello all,
I am performing transient simulation of a rectangular Natural Circulation loop operating between two temperatures of 299K-339K. I have given the operating temperature as average of the above mentioned temperature and o/p press is 90 bar. Fluid is CO2. After the simulation is run for a few iterations, it shows an error(see the attachment)--> "Primitive Error at Node 0: REFPROP_error (203) from function: tprho (density) Primitive Error at Node 1: REFPROP_error (203) from function: tprho (density) [TPRHO error 203] vapor iteration has not converged for T = 299.42 K, P = 7.1370 MPa, rho (last guess) = 6.6129 mol/L, x (mol frac) = 1.00000 [TPRHO error 203] vapor iteration has not converged for T = 299.29 K, P = 7.1370 MPa, rho (last guess) = 6.5994 mol/L, x (mol frac) = 1.00000 WHAT might be causing this? Any help is appreciated. Thanks |
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#2 |
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New Member
Hossein
Join Date: Apr 2013
Posts: 20
Rep Power: 14 ![]() |
Anybody here
Hello Does anybody know the solution? |
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#3 |
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New Member
Senthilkumar
Join Date: Oct 2012
Posts: 29
Rep Power: 15 ![]() |
I am surprised this question is still not answered.
If anybody have solution to this problem, it will be helpful. I am simulating a supersonic flow of supercritical CO2 through convergent divergent nozzle. Inlet condition Inlet : Pressure Inlet ;P0 = 95.7 bar T0 = 315K Real gas model : NIST |
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