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Issue with min/max rho chtMultiRegionSimpleFoam |
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November 19, 2019, 02:02 |
Issue with min/max rho chtMultiRegionSimpleFoam
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#1 |
Member
Ashish Magar
Join Date: Jul 2016
Location: Mumbai, India
Posts: 81
Rep Power: 10 |
Hello everyone,
I am trying to simulate a heat exchanger problem. I have split regions (3 regions, hot fluid cold fluid and solid) and defined corresponding properties in them. However while solving, the rho values in the output shows that it is not taking the values I am providing: Code:
Solving for fluid region shellSide DILUPBiCGStab: Solving for Ux, Initial residual = 1, Final residual = 0.0136616, No Iterations 1 DILUPBiCGStab: Solving for Uy, Initial residual = 1, Final residual = 0.0130695, No Iterations 1 DILUPBiCGStab: Solving for Uz, Initial residual = 1, Final residual = 0.0095, No Iterations 1 DILUPBiCGStab: Solving for h, Initial residual = 1, Final residual = 0.0350493, No Iterations 1 Min/max T:300 300.011 GAMG: Solving for p_rgh, Initial residual = 0.988378, Final residual = 0.00910654, No Iterations 4 time step continuity errors : sum local = 1856.54, global = -13.9992, cumulative = -13.9992 Min/max rho:2 2 Solving for fluid region tubeSide DILUPBiCGStab: Solving for Ux, Initial residual = 1, Final residual = 0.00932655, No Iterations 1 DILUPBiCGStab: Solving for Uy, Initial residual = 1, Final residual = 0.0102043, No Iterations 1 DILUPBiCGStab: Solving for Uz, Initial residual = 1, Final residual = 0.00692628, No Iterations 1 DILUPBiCGStab: Solving for h, Initial residual = 1, Final residual = 0.000374168, No Iterations 1 Min/max T:300 350 GAMG: Solving for p_rgh, Initial residual = 0.985978, Final residual = 0.00349933, No Iterations 5 time step continuity errors : sum local = 991.807, global = -31.1576, cumulative = -45.1567 Min/max rho:2 2 This is just the first iteration and then I stopped. This is the thermophysicalProperties file: Code:
thermoType { type heRhoThermo; mixture pureMixture; transport const; thermo hConst; equationOfState perfectFluid; specie specie; energy sensibleEnthalpy; } mixture { specie { nMoles 1; molWeight 18.0; // [g/mol] } equationOfState { R 3000; // [J/(kg K)] rho0 996; // [kg/m^3] } thermodynamics { Cp 4179; // [J/(kg K)] at T = 293 K Hf 0; } transport { mu 0.000852; // [kg/(m s)] Pr 0.7; } } Thanks for any suggestions. |
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November 19, 2019, 09:17 |
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#2 |
Member
Ashish Magar
Join Date: Jul 2016
Location: Mumbai, India
Posts: 81
Rep Power: 10 |
Alright. I solved it by myself.
In the system/regions/fvSolution was: Code:
... momentumPredictor yes; nNonOrthogonalCorrectors 0; pRefCell 0; pRefValue 100000; rhoMin 0.2; rhoMax 2; ... Code:
... momentumPredictor yes; nNonOrthogonalCorrectors 0; pRefCell 0; pRefValue 100000; rhoMin 900; rhoMax 1000; ... Thanks. |
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