|
[Sponsors] |
August 23, 2024, 10:15 |
KIND_SCALAR_MODEL, mixture
|
#1 |
New Member
Giovanni Bettega
Join Date: Sep 2014
Posts: 16
Rep Power: 12 |
Hello forum,
a mixture of three components: see below, with species transport active. % ------------------------------------------ % Fluid mixture definition % ------------------------------------------ FLUID_MODEL= FLUID_MIXTURE INC_DENSITY_MODEL= VARIABLE INC_ENERGY_EQUATION= YES MOLECULAR_WEIGHT= ( 28.964700, 28.964700, 28.964700 ) SPECIFIC_HEAT_CP= ( 1004.700000, 1004.700000, 1004.700000 ) % ------------------------------------------ % Mixture thermal conductivity model % ------------------------------------------ CONDUCTIVITY_MODEL= CONSTANT_PRANDTL PRANDTL_LAM= ( 0.710000, 0.710000, 0.710000 ) PRANDTL_TURB= ( 0.900000, 0.900000, 0.900000 ) TURBULENT_CONDUCTIVITY_MODEL= CONSTANT_PRANDTL_TURB % ------------------------------------------ % Mixture viscosity model % ------------------------------------------ VISCOSITY_MODEL= CONSTANT_VISCOSITY MU_CONSTANT= ( 0.000017, 0.000017, 0.000017 ) MIXING_VISCOSITY_MODEL= WILKE KIND_SCALAR_MODEL= SPECIES_TRANSPORT %KIND_SCALAR_MODEL= NONE % ------------------------------------------ % Mixture diffusivity model % ------------------------------------------ DIFFUSIVITY_MODEL= CONSTANT_DIFFUSIVITY DIFFUSIVITY_CONSTANT= 0.001000 CONV_NUM_METHOD_SPECIES= BOUNDED_SCALAR MUSCL_SPECIES= NO SLOPE_LIMITER_SPECIES= NONE TIME_DISCRE_SPECIES= EULER_IMPLICIT CFL_REDUCTION_SPECIES= 1.0 SPECIES_INIT= ( 0.333333, 0.333333 ) SPECIES_CLIPPING= NO SPECIES_CLIPPING_MAX= ( 1.0, 1.0 ) SPECIES_CLIPPING_MIN= ( 0.0, 0.0 ) Now, KIND_SCALAR_MODEL= SPECIES_TRANSPORT needs SPECIES_INIT= ( 0.333333, 0.333333 ) If I use (commenting SPECIES_INIT) KIND_SCALAR_MODEL= NONE %SPECIES_INIT= ( 0.333333, 0.333333 ) the solver outputs an error, Error in "void CConfig::SetPostprocessing(SU2_COMPONENT, short unsigned int, short unsigned int)": ------------------------------------------------------------------------- The use of FLUID_MIXTURE requires the number of entries for MOLECULAR_WEIGHT and SPECIFIC_HEAT_CP, to be equal to the number of entries of SPECIES_INIT + 1 ------------------------------ Error Exit ------------------------------- Now, if I use (reactivate SPECIES_INIT) KIND_SCALAR_MODEL= NONE SPECIES_INIT= ( 0.333333, 0.333333 ) the solver runs and reaches a certain convergence level. Species_0 Diffusivity_0, Species_1 Diffusivity_1 are removed from the results output. KIND_SCALAR_MODEL is NONE (off) and FLUID_MODEL= FLUID_MIXTURE Quqestion: what's happening? Which fluid is SU2 simulating? A mixture, one component of the mixture? Grazie mille Giovanni Last edited by gbettega; August 23, 2024 at 11:26. |
|
August 26, 2024, 06:58 |
|
#2 | |
New Member
Join Date: Feb 2022
Posts: 20
Rep Power: 5 |
Quote:
Thank you so much for your question, when the KIND_SCALAR_MODEL=NONE, it means that you are not solving the species transport equations, that is why you do not get the following output: Species_0 Diffusivity_0, Species_1 Diffusivity_1 In this case, the fluid model used is the default, which is CONTANT_DENSITY for incompressible flows, and you can check that the density output is the value of the constant density provided in the option INC_DENSITY_INIT. I hope this helps, please let me know if you have any other doubt. Best regards, Cristopher Morales Ubal |
||
August 26, 2024, 09:04 |
|
#3 |
New Member
Giovanni Bettega
Join Date: Sep 2014
Posts: 16
Rep Power: 12 |
Thanks a lot Cristopher
for your support. I didn't read the code, so it was unclear for me that the solution without species transport active referred to default fluid. I needed it for tuning a Su2 GUI. Regars Giovanni |
|
Tags |
mixture model, species tranport |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Setup Two-Phase Mixture for Ejector Modeling | mostic | CFX | 2 | January 10, 2022 18:09 |
Creating mixture material for gas dissolved in liquid | richard222 | Fluent Multiphase | 0 | May 7, 2016 14:20 |
Mixture model + VOF? | blacksoil2012 | Fluent Multiphase | 2 | February 9, 2014 00:59 |
mixture mass continuity eqn v.s. volumetric mixture continuity eqn | kaifu | ANSYS | 0 | June 9, 2011 09:42 |
mixture mass continuity v.s. volumetric mixture continuity in pressure equation | kaifu | OpenFOAM | 0 | June 9, 2011 09:14 |