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| 1 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 2 | +% % |
| 3 | +% SU2 configuration file % |
| 4 | +% Case description: 2D Cylinder Interface (Mixing Plane) % |
| 5 | +% Author: J. Kelly % |
| 6 | +% Institution: University of Liverpool % |
| 7 | +% Date: Dec 1st, 2025 % |
| 8 | +% File Version 8.3.0 "Harrier" % |
| 9 | +% % |
| 10 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 11 | +% |
| 12 | +MULTIZONE= YES |
| 13 | +CONFIG_LIST= (zone_1.cfg, zone_2.cfg) |
| 14 | +% |
| 15 | +% ------------- DIRECT, ADJOINT, AND LINEARIZED PROBLEM DEFINITION ------------% |
| 16 | +% |
| 17 | +SOLVER= RANS |
| 18 | +KIND_TURB_MODEL= SA |
| 19 | +READ_BINARY_RESTART=NO |
| 20 | +MATH_PROBLEM= DISCRETE_ADJOINT |
| 21 | +% |
| 22 | +% -------------------- COMPRESSIBLE FREE-STREAM DEFINITION --------------------% |
| 23 | +% |
| 24 | +MACH_NUMBER= 0.05 |
| 25 | +AOA= 0.0 |
| 26 | +FREESTREAM_PRESSURE= 1E6 |
| 27 | +FREESTREAM_TEMPERATURE= 300.0 |
| 28 | +FREESTREAM_DENSITY= 1.7418 |
| 29 | +FREESTREAM_OPTION= TEMPERATURE_FS |
| 30 | +FREESTREAM_TURBULENCEINTENSITY = 0.03 |
| 31 | +FREESTREAM_TURB2LAMVISCRATIO = 100.0 |
| 32 | +INIT_OPTION= TD_CONDITIONS |
| 33 | +% |
| 34 | +% ---------------------- REFERENCE VALUE DEFINITION ---------------------------% |
| 35 | +% |
| 36 | +REF_ORIGIN_MOMENT_X = 0.00 |
| 37 | +REF_ORIGIN_MOMENT_Y = 0.00 |
| 38 | +REF_ORIGIN_MOMENT_Z = 0.00 |
| 39 | +REF_LENGTH= 1.0 |
| 40 | +REF_AREA= 1.0 |
| 41 | +REF_DIMENSIONALIZATION= DIMENSIONAL |
| 42 | +% |
| 43 | +% ------------------------------ EQUATION OF STATE ----------------------------% |
| 44 | +% |
| 45 | +FLUID_MODEL= IDEAL_GAS |
| 46 | +GAMMA_VALUE= 1.4 |
| 47 | +GAS_CONSTANT= 287.058 |
| 48 | +% |
| 49 | +% --------------------------- VISCOSITY MODEL ---------------------------------% |
| 50 | +% |
| 51 | +VISCOSITY_MODEL= CONSTANT_VISCOSITY |
| 52 | +MU_REF= 1.716E-5 |
| 53 | +MU_T_REF= 273.15 |
| 54 | +SUTHERLAND_CONSTANT= 110.4 |
| 55 | +% |
| 56 | +% --------------------------- THERMAL CONDUCTIVITY MODEL ----------------------% |
| 57 | +% |
| 58 | +CONDUCTIVITY_MODEL= CONSTANT_PRANDTL |
| 59 | +% |
| 60 | +% -------------------- BOUNDARY CONDITION DEFINITION --------------------------% |
| 61 | +% |
| 62 | +%MARKER_EULER = (INFLOW, INMIX, OUTMIX, OUTFLOW, CIRC1, CIRC2) |
| 63 | +MARKER_HEATFLUX= ( CIRC1, 0.0, CIRC2, 0.0) |
| 64 | +% |
| 65 | +MARKER_PERIODIC= ( PER1, PER2, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 20.0, 0.0, PER3, PER4, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 20.0, 0.0) |
| 66 | +% |
| 67 | +%-------- INFLOW/OUTFLOW BOUNDARY CONDITION SPECIFIC FOR TURBOMACHINERY --------% |
| 68 | +% |
| 69 | +% Inflow and Outflow markers must be specified, for each blade (zone), following the natural groth of the machine (i.e, from the first blade to the last) |
| 70 | +MARKER_TURBOMACHINERY= (INFLOW, OUTMIX, INMIX, OUTFLOW) |
| 71 | +% |
| 72 | +MARKER_ZONE_INTERFACE= (OUTMIX, INMIX) |
| 73 | +% Mixing-plane interface markers must be specified to activate the transfer of information between zones |
| 74 | +MARKER_MIXINGPLANE_INTERFACE= (OUTMIX, INMIX) |
| 75 | +% |
| 76 | +MARKER_GILES= (INFLOW, TOTAL_CONDITIONS_PT, 1E6, 300, 1.0, 0.0, 0.0,1.0,1.0, OUTMIX, MIXING_OUT, 0.0, 0.0, 0.0, 0.0, 0.0,1.0,1.0, INMIX, MIXING_IN, 0.0, 0.0, 0.0, 0.0, 0.0,1.0, 1.0, OUTFLOW, STATIC_PRESSURE, 9E5, 0.0, 0.0, 0.0, 0.0,1.0,1.0) |
| 77 | +SPATIAL_FOURIER= YES |
| 78 | +% |
| 79 | +% |
| 80 | +%---------------------------- TURBOMACHINERY SIMULATION -----------------------------% |
| 81 | +% |
| 82 | +TURBOMACHINERY_KIND= AXIAL AXIAL |
| 83 | +TURBO_PERF_KIND = TURBINE TURBINE |
| 84 | +TURBULENT_MIXINGPLANE= YES |
| 85 | +AVERAGE_PROCESS_KIND= MIXEDOUT |
| 86 | +PERFORMANCE_AVERAGE_PROCESS_KIND= MIXEDOUT |
| 87 | +MIXEDOUT_COEFF= (1.0, 1.0E-05, 15) |
| 88 | +AVERAGE_MACH_LIMIT= 0.05 |
| 89 | +% |
| 90 | +% ------------------------ SURFACES IDENTIFICATION ----------------------------% |
| 91 | +% |
| 92 | +MARKER_PLOTTING= CIRC1, CIRC2 |
| 93 | +MARKER_MONITORING= CIRC1, CIRC2 |
| 94 | +MARKER_DESIGNING= CIRC1, CIRC2 |
| 95 | +MARKER_ANALYZE= CIRC1, CIRC2 |
| 96 | +% |
| 97 | +% ------------- COMMON PARAMETERS DEFINING THE NUMERICAL METHOD ---------------% |
| 98 | +% |
| 99 | +NUM_METHOD_GRAD= WEIGHTED_LEAST_SQUARES |
| 100 | +CFL_NUMBER= 10.0 |
| 101 | +CFL_ADAPT= NO |
| 102 | +CFL_ADAPT_PARAM= ( 1.3, 1.2, 1.0, 10.0) |
| 103 | +% |
| 104 | +% ------------------------ LINEAR SOLVER DEFINITION ---------------------------% |
| 105 | +% |
| 106 | +LINEAR_SOLVER= FGMRES |
| 107 | +LINEAR_SOLVER_PREC= LU_SGS |
| 108 | +LINEAR_SOLVER_ERROR= 1E-4 |
| 109 | +LINEAR_SOLVER_ITER= 20 |
| 110 | +% |
| 111 | +% ---------- NOT WORKING WITH PERIODIC BOUNDARY CONDITIONS !!!!! --------------% |
| 112 | +% |
| 113 | +% |
| 114 | +% ----------------------- SLOPE LIMITER DEFINITION ----------------------------% |
| 115 | +% |
| 116 | +VENKAT_LIMITER_COEFF= 0.05 |
| 117 | +LIMITER_ITER= 999999 |
| 118 | +% |
| 119 | +% -------------------- FLOW NUMERICAL METHOD DEFINITION -----------------------% |
| 120 | +% |
| 121 | +CONV_NUM_METHOD_FLOW= ROE |
| 122 | +MUSCL_FLOW= NO |
| 123 | +SLOPE_LIMITER_FLOW= VAN_ALBADA_EDGE |
| 124 | +ENTROPY_FIX_COEFF= 0.1 |
| 125 | +JST_SENSOR_COEFF= ( 0.5, 0.02 ) |
| 126 | +TIME_DISCRE_FLOW= EULER_IMPLICIT |
| 127 | +% |
| 128 | +% -------------------- TURBULENT NUMERICAL METHOD DEFINITION ------------------% |
| 129 | +% |
| 130 | +CONV_NUM_METHOD_TURB= SCALAR_UPWIND |
| 131 | +MUSCL_TURB= NO |
| 132 | +SLOPE_LIMITER_TURB= VENKATAKRISHNAN |
| 133 | +TIME_DISCRE_TURB= EULER_IMPLICIT |
| 134 | +CFL_REDUCTION_TURB= 1.0 |
| 135 | +% |
| 136 | +% ----------------------- DESIGN VARIABLE PARAMETERS --------------------------% |
| 137 | +% |
| 138 | +%DV_KIND= FFD_SETTING |
| 139 | +%DV_MARKER= (CIRC1, CIRC2) |
| 140 | +%DV_PARAM= ( CIRC1, 1, 0, 0, 0.0, 1.0, 0.0 ) |
| 141 | +%DV_VALUE= 0.001 |
| 142 | +% |
| 143 | +DV_KIND= FFD_CONTROL_POINT_2D, FFD_CONTROL_POINT_2D, FFD_CONTROL_POINT_2D, FFD_CONTROL_POINT_2D |
| 144 | +DV_MARKER= ( CIRC1, CIRC2 ) |
| 145 | +DV_PARAM=( CIRCLE1, 0, 0, 1.0, 0.0 );( CIRCLE2, 0, 0, 1.0, 0.0 );( CIRCLE1, 1, 1, 1.0, 0.0 );( CIRCLE2, 1, 1, 1.0, 0.0 ) |
| 146 | +DV_VALUE=0.0,0.0,0.0,0.0 |
| 147 | +% |
| 148 | +% ------------------------ GRID DEFORMATION PARAMETERS ------------------------% |
| 149 | +% |
| 150 | +% Linear solver or smoother for implicit formulations (FGMRES, RESTARTED_FGMRES, BCGSTAB) |
| 151 | +DEFORM_LINEAR_SOLVER= FGMRES |
| 152 | +% |
| 153 | +% Preconditioner of the Krylov linear solver (ILU, LU_SGS, JACOBI) |
| 154 | +DEFORM_LINEAR_SOLVER_PREC= ILU |
| 155 | +% |
| 156 | +% Number of smoothing iterations for mesh deformation |
| 157 | +DEFORM_LINEAR_SOLVER_ITER= 1000 |
| 158 | +% |
| 159 | +% Number of nonlinear deformation iterations (surface deformation increments) |
| 160 | +DEFORM_NONLINEAR_ITER= 1 |
| 161 | +% |
| 162 | +% Minimum residual criteria for the linear solver convergence of grid deformation |
| 163 | +DEFORM_LINEAR_SOLVER_ERROR= 1E-14 |
| 164 | +% |
| 165 | +% Print the residuals during mesh deformation to the console (YES, NO) |
| 166 | +DEFORM_CONSOLE_OUTPUT= YES |
| 167 | +% |
| 168 | +% Type of element stiffness imposed for FEA mesh deformation (INVERSE_VOLUME, |
| 169 | +% WALL_DISTANCE, CONSTANT_STIFFNESS) |
| 170 | +DEFORM_STIFFNESS_TYPE= WALL_DISTANCE |
| 171 | +% |
| 172 | +% |
| 173 | +% -------------------- FREE-FORM DEFORMATION PARAMETERS -----------------------% |
| 174 | +% |
| 175 | +FFD_TOLERANCE= 1E-10 |
| 176 | +FFD_ITERATIONS= 500 |
| 177 | +FFD_DEFINITION= (CIRCLE1, -2.0, -2.0, 0.0, 2.0, -2.0, 0.0, 2.0, 2.0, 0.0, -2.0, 2.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0); (CIRCLE2, 18.0, -2.0, 0.0, 22.0, -2.0, 0.0, 22.0, 2.0, 0.0, 18.0, 2.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0, 0.0) |
| 178 | +FFD_DEGREE= ( 2 , 2 , 0 ); (2, 2, 0) |
| 179 | +FFD_CONTINUITY= 2ND_DERIVATIVE |
| 180 | +% |
| 181 | +% --------------------- OPTIMAL SHAPE DESIGN DEFINITION -----------------------% |
| 182 | +% |
| 183 | +% FFD_CONTROL_POINT_2D |
| 184 | +DEFINITION_DV= ( 19, 1.0 | CIRC1 | CIRCLE1, 0, 0, 1.0, 0.0 ); ( 19, 1.0 | CIRC2 | CIRCLE2, 0, 0, 1.0, 0.0 ); ( 19, 1.0 | CIRC1 | CIRCLE1, 1, 1, 1.0, 0.0 ); ( 19, 1.0 | CIRC2 | CIRCLE2, 1, 1, 1.0, 0.0 ); |
| 185 | +OPT_OBJECTIVE= ENTROPY_GENERATION* 0.0001 |
| 186 | +OPT_ITERATIONS= 19 |
| 187 | +OPT_ACCURACY= 1E-10 |
| 188 | +% |
| 189 | +% --------------------- OBJECTIVE FUNCTION DEFINITION -----------------------% |
| 190 | +% |
| 191 | +OBJECTIVE_FUNCTION= ENTROPY_GENERATION |
| 192 | +% |
| 193 | +% ------------------------- CONVERGENCE PARAMETERS --------------------------% |
| 194 | +% |
| 195 | +OUTER_ITER= 201 |
| 196 | +CONV_RESIDUAL_MINVAL= -16 |
| 197 | +CONV_STARTITER= 10 |
| 198 | +CONV_CAUCHY_ELEMS= 100 |
| 199 | +CONV_CAUCHY_EPS= 1E-6 |
| 200 | +% |
| 201 | +% ------------------------- INPUT/OUTPUT INFORMATION --------------------------% |
| 202 | +% |
| 203 | +SCREEN_OUTPUT= OUTER_ITER, AVG_BGS_RES[0], AVG_BGS_RES[1], RMS_DENSITY[0], RMS_ENERGY[0], RMS_DENSITY[1], RMS_ENERGY[1], COMBO |
| 204 | +HISTORY_OUTPUT= ITER, RMS_RES, COMBO |
| 205 | +MESH_FILENAME= circ_out.su2 |
| 206 | +MESH_FORMAT= SU2 |
| 207 | +MESH_OUT_FILENAME= mesh_out.su2 |
| 208 | +SOLUTION_FILENAME= solution_flow |
| 209 | +SOLUTION_ADJ_FILENAME= solution_adj |
| 210 | +TABULAR_FORMAT= CSV |
| 211 | +OUTPUT_FILES= RESTART_ASCII, TECPLOT, SURFACE_TECPLOT |
| 212 | +CONV_FILENAME= history |
| 213 | +RESTART_FILENAME= restart_flow |
| 214 | +RESTART_ADJ_FILENAME= restart_adj |
| 215 | +VOLUME_FILENAME= flow |
| 216 | +VOLUME_ADJ_FILENAME= adjoint |
| 217 | +GRAD_OBJFUNC_FILENAME= of_grad.dat |
| 218 | +SURFACE_FILENAME= surface_flow |
| 219 | +SURFACE_ADJ_FILENAME= surface_adjoint |
| 220 | +SURFACE_SENS_FILENAME= surface_sens |
| 221 | +WRT_ZONE_CONV= NO |
| 222 | +WRT_ZONE_HIST= YES |
| 223 | +OUTPUT_PRECISION= 16 |
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