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| 1 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 2 | +% % |
| 3 | +% SU2 configuration file % |
| 4 | +% Case description: Axisymmetric supersonic converging-diverging air nozzle % |
| 5 | +% Author: Florian Dittmann % |
| 6 | +% Date: 2021.12.02 % |
| 7 | +% File Version 7.4.0 "Blackbird" % |
| 8 | +% % |
| 9 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 10 | +% |
| 11 | +% ------------- DIRECT, ADJOINT, AND LINEARIZED PROBLEM DEFINITION ------------% |
| 12 | +% |
| 13 | +SOLVER= RANS |
| 14 | +KIND_TURB_MODEL= SST |
| 15 | +RESTART_SOL= YES |
| 16 | +% |
| 17 | +AXISYMMETRIC= YES |
| 18 | +% |
| 19 | +% -------------------- COMPRESSIBLE FREE-STREAM DEFINITION --------------------% |
| 20 | +% |
| 21 | +MACH_NUMBER= 1E-9 |
| 22 | +% |
| 23 | +INIT_OPTION= TD_CONDITIONS |
| 24 | +% |
| 25 | +FREESTREAM_OPTION= TEMPERATURE_FS |
| 26 | +FREESTREAM_PRESSURE= 1400000 |
| 27 | +FREESTREAM_TEMPERATURE= 373.15 |
| 28 | +% |
| 29 | +REF_DIMENSIONALIZATION= DIMENSIONAL |
| 30 | +% |
| 31 | +% ---- IDEAL GAS, POLYTROPIC, VAN DER WAALS AND PENG ROBINSON CONSTANTS -------% |
| 32 | +% |
| 33 | +FLUID_MODEL= STANDARD_AIR |
| 34 | +% |
| 35 | +% --------------------------- VISCOSITY MODEL ---------------------------------% |
| 36 | +% |
| 37 | +VISCOSITY_MODEL= CONSTANT_VISCOSITY |
| 38 | +MU_CONSTANT= 1.716E-5 |
| 39 | +% |
| 40 | +% --------------------------- THERMAL CONDUCTIVITY MODEL ----------------------% |
| 41 | +% |
| 42 | +CONDUCTIVITY_MODEL= CONSTANT_PRANDTL |
| 43 | +PRANDTL_LAM= 0.72 |
| 44 | +PRANDTL_TURB= 0.90 |
| 45 | +% |
| 46 | +% -------------------- BOUNDARY CONDITION DEFINITION --------------------------% |
| 47 | +% |
| 48 | +MARKER_HEATFLUX= ( WALL, 0.0 ) |
| 49 | +MARKER_SYM= ( SYMMETRY ) |
| 50 | +MARKER_RIEMANN= ( INFLOW, TOTAL_CONDITIONS_PT, 1400000.0, 373.15, 1.0, 0.0, 0.0, \ |
| 51 | + OUTFLOW, STATIC_PRESSURE, 100000.0, 0.0, 0.0, 0.0, 0.0 ) |
| 52 | +MARKER_MONITORING = (WALL) |
| 53 | + |
| 54 | +% ------------- COMMON PARAMETERS DEFINING THE NUMERICAL METHOD ---------------% |
| 55 | +% |
| 56 | +NUM_METHOD_GRAD= GREEN_GAUSS |
| 57 | +CFL_NUMBER= 1000.0 |
| 58 | +CFL_ADAPT= NO |
| 59 | +MAX_DELTA_TIME= 1E6 |
| 60 | +OBJECTIVE_FUNCTION= DRAG |
| 61 | +% |
| 62 | +% ----------- SLOPE LIMITER AND DISSIPATION SENSOR DEFINITION -----------------% |
| 63 | +% |
| 64 | +MUSCL_FLOW= YES |
| 65 | +SLOPE_LIMITER_FLOW= NONE |
| 66 | +% |
| 67 | +% ------------------------ LINEAR SOLVER DEFINITION ---------------------------% |
| 68 | +% |
| 69 | +LINEAR_SOLVER= FGMRES |
| 70 | +LINEAR_SOLVER_PREC= ILU |
| 71 | +LINEAR_SOLVER_ILU_FILL_IN= 0 |
| 72 | +LINEAR_SOLVER_ERROR= 0.01 |
| 73 | +LINEAR_SOLVER_ITER= 10 |
| 74 | +% |
| 75 | +% -------------------- FLOW NUMERICAL METHOD DEFINITION -----------------------% |
| 76 | +% |
| 77 | +CONV_NUM_METHOD_FLOW= ROE |
| 78 | +ENTROPY_FIX_COEFF= 0.1 |
| 79 | +TIME_DISCRE_FLOW= EULER_IMPLICIT |
| 80 | +% |
| 81 | +% -------------------- TURBULENT NUMERICAL METHOD DEFINITION ------------------% |
| 82 | +% |
| 83 | +CONV_NUM_METHOD_TURB= SCALAR_UPWIND |
| 84 | +TIME_DISCRE_TURB= EULER_IMPLICIT |
| 85 | +CFL_REDUCTION_TURB= 1.0 |
| 86 | +% |
| 87 | +% --------------------------- CONVERGENCE PARAMETERS --------------------------% |
| 88 | +% |
| 89 | +ITER= 1000 |
| 90 | +CONV_RESIDUAL_MINVAL= -12 |
| 91 | +CONV_STARTITER= 10 |
| 92 | +% |
| 93 | +% ------------------------- INPUT/OUTPUT INFORMATION --------------------------% |
| 94 | +% |
| 95 | +MESH_FILENAME= nozzle.su2 |
| 96 | +% |
| 97 | +SOLUTION_FILENAME= restart_flow.dat |
| 98 | +RESTART_FILENAME= restart_flow.dat |
| 99 | +OUTPUT_WRT_FREQ= 1000 |
| 100 | +% |
| 101 | +% Note: This cfg is used for a primal and adjoint Testcase, therefore both residuals are present here. |
| 102 | +SCREEN_OUTPUT= (INNER_ITER, RMS_DENSITY, RMS_ENERGY, RMS_TKE, RMS_DISSIPATION, TOTAL_HEATFLUX, \ |
| 103 | + RMS_ADJ_DENSITY, RMS_ADJ_ENERGY, RMS_ADJ_TKE, RMS_ADJ_DISSIPATION, SENS_AOA, SENS_MACH) |
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