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Merge pull request #2271 from sun5k/feature_Compressibility_Correction
Compressibility correction for SST model
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TestCases/rans/flatplate/turb_SST_flatplate_compressibility_Sarkar.cfg
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%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% | ||
% % | ||
% SU2 configuration file % | ||
% Case description: Turbulent flow over flat plate(2DZPH) % | ||
% Author: Sunoh. Kang % | ||
% Institution: Pusan National University % | ||
% Date: 2024.04.30 % | ||
% File Version 8.0.1 "Harrier" % | ||
% % | ||
%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% | ||
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% ------------- DIRECT, ADJOINT, AND LINEARIZED PROBLEM DEFINITION ------------% | ||
% | ||
SOLVER= RANS | ||
KIND_TURB_MODEL= SST | ||
SST_OPTIONS= V2003m, COMPRESSIBILITY-SARKAR | ||
MATH_PROBLEM= DIRECT | ||
RESTART_SOL= NO | ||
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% ------------------------ COMPRESSIBLE FREE-STREAM DEFINITION ----------------% | ||
% | ||
MACH_NUMBER= 5.0 | ||
AOA= 0.000 | ||
INIT_OPTION= TD_CONDITIONS | ||
FREESTREAM_OPTION= TEMPERATURE_FS | ||
FREESTREAM_TEMPERATURE= 300.3333 | ||
FREESTREAM_PRESSURE= 13753.90558 | ||
FREESTREAM_TURBULENCEINTENSITY = 0.00002 | ||
FREESTREAM_TURB2LAMVISCRATIO = 0.009 | ||
REF_DIMENSIONALIZATION= DIMENSIONAL | ||
REYNOLDS_NUMBER= 15E6 | ||
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||
% ---- IDEAL GAS, POLYTPOPIC, VAN DER WALLS AND PENG ROBINSOPN CNSTANTS ------ % | ||
% | ||
FLUID_MODEL= IDEAL_GAS | ||
GAMMA_VALUE= 1.4 | ||
GAS_CONSTANT= 287.058 | ||
ACENTRIC_FACTOR= 0.035 | ||
SPECIFIC_HEAT_CP= 1004.703 | ||
THERMAL_EXPANSION_COEFF= 0.00347 | ||
MOLECULAR_WEIGHT= 28.96 | ||
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% --------------------------- VISCOSITY MODEL ---------------------------------% | ||
% | ||
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VISCOSITY_MODEL= SUTHERLAND | ||
MU_REF= 1.716E-5 | ||
MU_T_REF= 273.15 | ||
SUTHERLAND_CONSTANT= 110.4 | ||
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% ------------------------ THERMAL CONDUCTIVITY MODEL -------------------------% | ||
% | ||
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CONDUCTIVITY_MODEL= CONSTANT_PRANDTL | ||
PRANDTL_LAM= 0.72 | ||
TURBULENT_CONDUCTIVITY_MODEL= CONSTANT_PRANDTL_TURB | ||
PRANDTL_TURB= 0.9 | ||
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% ---------------------- REFERENCE VALUE DEFINITION ---------------------------% | ||
% | ||
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REF_ORIGIN_MOMENT_X = 0.00 | ||
REF_ORIGIN_MOMENT_Y = 0.00 | ||
REF_ORIGIN_MOMENT_Z = 0.00 | ||
REF_LENGTH= 1.0 | ||
REF_AREA= 1.0 | ||
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% -------------------- BOUNDARY CONDITION DEFINITION --------------------------% | ||
% | ||
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MARKER_PLOTTING = ( wall ) | ||
MARKER_SUPERSONIC_INLET= ( inlet, 300.3333 , 13753.90558 , 1737.082226 , 0.0 , 0.0 ) | ||
MARKER_FAR= ( farfield ) | ||
MARKER_SYM= ( symmetry ) | ||
MARKER_SUPERSONIC_OUTLET= (outlet, 34384.76396) | ||
MARKER_ISOTHERMAL= ( wall, 327.36297) | ||
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% ------------- COMMON PARAMETERS DEFINING THE NUMERICAL METHOD ---------------% | ||
% | ||
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NUM_METHOD_GRAD= WEIGHTED_LEAST_SQUARES | ||
CFL_NUMBER= 0.5 | ||
CFL_ADAPT= YES | ||
CFL_ADAPT_PARAM= ( 0.1, 1.5, 0.5, 50.0 ) | ||
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% --------- SLOPE LIMITER DEFINITION, DISSIPATION SENSOR DEFINITION -----------------% | ||
% | ||
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MUSCL_FLOW= YES | ||
SLOPE_LIMITER_FLOW= VENKATAKRISHNAN_WANG | ||
SLOPE_LIMITER_TURB= NONE | ||
VENKAT_LIMITER_COEFF= 0.05 | ||
JST_SENSOR_COEFF= (0.5, 0.02) | ||
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% ------------------------ LINEAR SOLVER DEFINITION ---------------------------% | ||
% | ||
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LINEAR_SOLVER= FGMRES | ||
LINEAR_SOLVER_PREC= LU_SGS | ||
LINEAR_SOLVER_ERROR= 1E-6 | ||
LINEAR_SOLVER_ITER= 5 | ||
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% -------------------- FLOW NUMERICAL METHOD DEFINITION -----------------------% | ||
% | ||
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CONV_NUM_METHOD_FLOW= AUSM | ||
TIME_DISCRE_FLOW= EULER_IMPLICIT | ||
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% -------------------- TURBULENT NUMERICAL METHOD DEFINITION ------------------% | ||
% | ||
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CONV_NUM_METHOD_TURB= SCALAR_UPWIND | ||
TIME_DISCRE_TURB= EULER_IMPLICIT | ||
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% ------------------------- SCREEN/HISTORY VOLUME OUTPUT --------------------------% | ||
% | ||
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SCREEN_OUTPUT= (INNER_ITER, RMS_DENSITY, RMS_MOMENTUM-X, RMS_MOMENTUM-Y, RMS_ENERGY, RMS_TKE, RMS_DISSIPATION) | ||
SCREEN_WRT_FREQ_INNER= 1 | ||
SCREEN_WRT_FREQ_OUTER= 1 | ||
SCREEN_WRT_FREQ_TIME= 1 | ||
HISTORY_WRT_FREQ_INNER= 1 | ||
HISTORY_WRT_FREQ_OUTER= 1 | ||
HISTORY_WRT_FREQ_TIME= 1 | ||
OUTPUT_WRT_FREQ= 1000 | ||
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% ------------------------- INPUT/OUTPUT FILE INFORMATION --------------------------% | ||
% | ||
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MESH_FILENAME= mesh_flatplate_turb_137x97.su2 | ||
MESH_FORMAT= SU2 | ||
MESH_OUT_FILENAME= mesh_out.su2 | ||
SOLUTION_FILENAME= restart_flow.dat | ||
SOLUTION_ADJ_FILENAME= solution_adj.dat | ||
OUTPUT_FILES= (RESTART, PARAVIEW, SURFACE_PARAVIEW, TECPLOT, SURFACE_TECPLOT, CSV, SURFACE_CSV ) | ||
CONV_FILENAME= history | ||
BREAKDOWN_FILENAME= forces_breakdown.dat | ||
RESTART_FILENAME= restart_flow.dat | ||
RESTART_ADJ_FILENAME= restart_adj.dat | ||
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% ------------------------------- SOLVER CONTROL ------------------------------% | ||
% | ||
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ITER= 100 | ||
OUTER_ITER= 1 | ||
TIME_ITER= 100 | ||
CONV_RESIDUAL_MINVAL= -14 | ||
CONV_STARTITER= 10 | ||
CONV_CAUCHY_ELEMS= 100 | ||
CONV_CAUCHY_EPS= 1E-10 |
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