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| 1 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 2 | +% % |
| 3 | +% SU2 configuration file % |
| 4 | +% Case description: Active transport 2 species: Hydrogen and air. % |
| 5 | +% 1 transport equation is being solved(For H2 in this case). % |
| 6 | +% Including temperature limits for energy equation. % |
| 7 | +% Author: Cristopher Morales Ubal % |
| 8 | +% Institution: Eindhoven University of Technology % |
| 9 | +% Date: 2025/09/20 % |
| 10 | +% File Version 8.0.1 "Harrier" % |
| 11 | +% % |
| 12 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 13 | + |
| 14 | +% ------------- DIRECT, ADJOINT, AND LINEARIZED PROBLEM DEFINITION ------------% |
| 15 | +% |
| 16 | +SOLVER= INC_NAVIER_STOKES |
| 17 | +KIND_TURB_MODEL= NONE |
| 18 | +% |
| 19 | +% ---------------- INCOMPRESSIBLE FLOW CONDITION DEFINITION -------------------% |
| 20 | +% |
| 21 | +INC_DENSITY_MODEL= VARIABLE |
| 22 | +INC_DENSITY_INIT= 0.0807 |
| 23 | +% |
| 24 | +INC_VELOCITY_INIT= ( 1.0, 0.0, 0.0 ) |
| 25 | +% |
| 26 | +INC_ENERGY_EQUATION= YES |
| 27 | +TEMPERATURE_LIMITS= 250, 400 |
| 28 | +INC_TEMPERATURE_INIT= 350.0 |
| 29 | +% |
| 30 | +INC_NONDIM= DIMENSIONAL |
| 31 | +% |
| 32 | +% -------------------- FLUID PROPERTIES ------------------------------------- % |
| 33 | +% |
| 34 | +FLUID_MODEL= FLUID_MIXTURE |
| 35 | +% |
| 36 | +THERMODYNAMIC_PRESSURE= 101325.0 |
| 37 | +% |
| 38 | +MOLECULAR_WEIGHT= 2.01588, 28.960 |
| 39 | +% |
| 40 | +SPECIFIC_HEAT_CP = 14310, 1009.39 |
| 41 | +% |
| 42 | +CONDUCTIVITY_MODEL= CONSTANT_CONDUCTIVITY |
| 43 | +THERMAL_CONDUCTIVITY_CONSTANT= 0.187, 0.0258 |
| 44 | +% |
| 45 | +PRANDTL_LAM= 0.72, 0.72 |
| 46 | +TURBULENT_CONDUCTIVITY_MODEL= NONE |
| 47 | +PRANDTL_TURB= 0.90, 0.90 |
| 48 | +% |
| 49 | +% --------------------------- VISCOSITY MODEL ---------------------------------% |
| 50 | +% |
| 51 | +VISCOSITY_MODEL= CONSTANT_VISCOSITY |
| 52 | +% |
| 53 | +MU_CONSTANT= 8.9E-06, 1.8551E-05 |
| 54 | +% |
| 55 | +MU_REF= 8.411E-05, 1.716E-05 |
| 56 | +% |
| 57 | +MU_T_REF= 273, 273 |
| 58 | +% |
| 59 | +SUTHERLAND_CONSTANT= 97, 111 |
| 60 | +% |
| 61 | +MIXING_VISCOSITY_MODEL = WILKE |
| 62 | +% |
| 63 | +% -------------------- BOUNDARY CONDITION DEFINITION --------------------------% |
| 64 | +% |
| 65 | +MARKER_SYM= ( top, bottom) |
| 66 | +% |
| 67 | +SPECIFIED_INLET_PROFILE= NO |
| 68 | +INLET_FILENAME= inlet_venturi.dat |
| 69 | +INC_INLET_TYPE= VELOCITY_INLET VELOCITY_INLET |
| 70 | +MARKER_INLET= ( gas_inlet, 350, 3.0, 1.0, 0.0, 0.0,\ |
| 71 | + air_inlet, 300, 1.0, 1.0, 0.0, 0.0 ) |
| 72 | +MARKER_INLET_SPECIES= (gas_inlet, 1.0, air_inlet, 0.0) |
| 73 | +% |
| 74 | +INC_OUTLET_TYPE= PRESSURE_OUTLET |
| 75 | +MARKER_OUTLET= ( outlet, 0.0 ) |
| 76 | +% |
| 77 | +% ------------- COMMON PARAMETERS DEFINING THE NUMERICAL METHOD ---------------% |
| 78 | +% |
| 79 | +NUM_METHOD_GRAD= WEIGHTED_LEAST_SQUARES |
| 80 | +% |
| 81 | +CFL_NUMBER= 20 |
| 82 | +CFL_REDUCTION_SPECIES= 1.0 |
| 83 | +CFL_REDUCTION_TURB= 1.0 |
| 84 | +% |
| 85 | +% Run commented Iter for good results |
| 86 | +ITER= 5000 |
| 87 | +% |
| 88 | +% ------------------------ LINEAR SOLVER DEFINITION ---------------------------% |
| 89 | +% |
| 90 | +LINEAR_SOLVER= FGMRES |
| 91 | +LINEAR_SOLVER_PREC= ILU |
| 92 | +LINEAR_SOLVER_ERROR= 1E-5 |
| 93 | +LINEAR_SOLVER_ITER= 10 |
| 94 | +% |
| 95 | +% -------------------- FLOW NUMERICAL METHOD DEFINITION -----------------------% |
| 96 | +% |
| 97 | +CONV_NUM_METHOD_FLOW= FDS |
| 98 | +MUSCL_FLOW= NO |
| 99 | +SLOPE_LIMITER_FLOW = NONE |
| 100 | +TIME_DISCRE_FLOW= EULER_IMPLICIT |
| 101 | +% |
| 102 | +% -------------------- SCALAR TRANSPORT ---------------------------------------% |
| 103 | +% |
| 104 | +KIND_SCALAR_MODEL= SPECIES_TRANSPORT |
| 105 | +% |
| 106 | +DIFFUSIVITY_MODEL = UNITY_LEWIS |
| 107 | +% |
| 108 | +CONV_NUM_METHOD_SPECIES= BOUNDED_SCALAR |
| 109 | +MUSCL_SPECIES= NO |
| 110 | +SLOPE_LIMITER_SPECIES = NONE |
| 111 | +% |
| 112 | +TIME_DISCRE_SPECIES= EULER_IMPLICIT |
| 113 | +% |
| 114 | +SPECIES_INIT= 1.0 |
| 115 | +SPECIES_CLIPPING= NO |
| 116 | +SPECIES_CLIPPING_MIN= 0.0 |
| 117 | +SPECIES_CLIPPING_MAX= 1.0 |
| 118 | +% |
| 119 | +% -------------------- TURBULENT TRANSPORT ---------------------------------------% |
| 120 | +% |
| 121 | +CONV_NUM_METHOD_TURB= BOUNDED_SCALAR |
| 122 | +MUSCL_TURB= NO |
| 123 | +% |
| 124 | +% --------------------------- CONVERGENCE PARAMETERS --------------------------% |
| 125 | +% |
| 126 | +CONV_FIELD= RMS_PRESSURE, RMS_VELOCITY-X, RMS_VELOCITY-Y, RMS_TKE, RMS_SPECIES |
| 127 | +CONV_RESIDUAL_MINVAL= -18 |
| 128 | +CONV_STARTITER= 10 |
| 129 | +% |
| 130 | +% ------------------------- INPUT/OUTPUT INFORMATION --------------------------% |
| 131 | +% |
| 132 | +MESH_FILENAME= rectangle_mixing.su2 |
| 133 | +SCREEN_OUTPUT= INNER_ITER WALL_TIME \ |
| 134 | + RMS_PRESSURE RMS_VELOCITY-X RMS_VELOCITY-Y RMS_ENTHALPY RMS_TKE RMS_DISSIPATION RMS_SPECIES_0 RMS_SPECIES_1 \ |
| 135 | + LINSOL_ITER LINSOL_RESIDUAL \ |
| 136 | + LINSOL_ITER_TURB LINSOL_RESIDUAL_TURB \ |
| 137 | + LINSOL_ITER_SPECIES LINSOL_RESIDUAL_SPECIES \ |
| 138 | + SURFACE_SPECIES_0 |
| 139 | +SCREEN_WRT_FREQ_INNER= 10 |
| 140 | +% |
| 141 | +HISTORY_OUTPUT= ITER RMS_RES LINSOL SPECIES_COEFF SPECIES_COEFF_SURF |
| 142 | +CONV_FILENAME= history |
| 143 | +MARKER_ANALYZE= gas_inlet, air_inlet, outlet |
| 144 | +MARKER_ANALYZE_AVERAGE= AREA |
| 145 | +% |
| 146 | +OUTPUT_FILES= RESTART_ASCII, PARAVIEW_MULTIBLOCK |
| 147 | +VOLUME_OUTPUT= RESIDUAL, PRIMITIVE |
| 148 | +OUTPUT_WRT_FREQ= 100 |
| 149 | +% |
| 150 | +RESTART_SOL= NO |
| 151 | +READ_BINARY_RESTART= NO |
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