CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > SU2

KIND_SCALAR_MODEL, mixture

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   August 23, 2024, 10:15
Default KIND_SCALAR_MODEL, mixture
  #1
New Member
 
Giovanni Bettega
Join Date: Sep 2014
Posts: 16
Rep Power: 12
gbettega is on a distinguished road
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.
gbettega is offline   Reply With Quote

Old   August 26, 2024, 06:58
Default
  #2
New Member
 
Join Date: Feb 2022
Posts: 20
Rep Power: 5
cristopher_morales is on a distinguished road
Quote:
Originally Posted by gbettega View Post
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
Hi Giovanni,

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
cristopher_morales is offline   Reply With Quote

Old   August 26, 2024, 09:04
Default
  #3
New Member
 
Giovanni Bettega
Join Date: Sep 2014
Posts: 16
Rep Power: 12
gbettega is on a distinguished road
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
gbettega is offline   Reply With Quote

Reply

Tags
mixture model, species tranport


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


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


All times are GMT -4. The time now is 18:22.