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| 1 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 2 | +% % |
| 3 | +% SU2 configuration file % |
| 4 | +% Case description: Turbulent flow, ONERA M6, Newton-Krylov solver % |
| 5 | +% File Version 7.1.0 "Blackbird" % |
| 6 | +% % |
| 7 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 8 | + |
| 9 | +SOLVER= RANS |
| 10 | +KIND_TURB_MODEL= SA |
| 11 | +MATH_PROBLEM= DIRECT |
| 12 | +RESTART_SOL= NO |
| 13 | + |
| 14 | +% ------------------------- NEWTON-KRYLOV PARAMETERS --------------------------% |
| 15 | +% |
| 16 | +% --- Things that matter --- |
| 17 | +NEWTON_KRYLOV= YES |
| 18 | + |
| 19 | +% Iterations and tolerance for the Krylov part, it is important not to |
| 20 | +% "over solve", tolerance should be as high as possible. |
| 21 | +LINEAR_SOLVER_ITER= 5 |
| 22 | +LINEAR_SOLVER_ERROR= 0.25 |
| 23 | + |
| 24 | +% For "n0" iterations or "r0" residual reduction, the normal quasi-Newton iterations |
| 25 | +% are used. Then, they become the preconditioner for the NK iterations with "np" linear |
| 26 | +% iterations or "tp" tolerance, with "np"=0 the linear preconditioner (e.g. ILU) is |
| 27 | +% used directly (this may be enough for unsteady). |
| 28 | +% The tolerance for NK iterations is initially relaxed by factor "ft", and reaches |
| 29 | +% LINEAR_SOLVER_ERROR after "rf" residual reduction (additional to "r0"). |
| 30 | +% The Jacobian-free products are based on finite differences with step "e". |
| 31 | +NEWTON_KRYLOV_IPARAM= (0, 3, 2) % n0, np, ft |
| 32 | +NEWTON_KRYLOV_DPARAM= (-1.0, 0.1, -6.0, 1e-5) % r0, tp, rf, e |
| 33 | + |
| 34 | +CFL_ADAPT= YES % it's needed |
| 35 | +CFL_NUMBER= 10 |
| 36 | +CFL_ADAPT_PARAM= ( 0.8, 1.1, 5, 1000 ) % no point using NK with low CFL values |
| 37 | +
|
| 38 | +% It is important (more than usual) to have similar magnitude variables |
| 39 | +REF_DIMENSIONALIZATION= FREESTREAM_VEL_EQ_MACH |
| 40 | +
|
| 41 | +USE_VECTORIZATION= YES % compile the code for AVX and mixed precision or it will be slow! |
| 42 | +TIME_DISCRE_FLOW= EULER_IMPLICIT % what else |
| 43 | +LINEAR_SOLVER_PREC= ILU % or LU_SGS |
| 44 | +
|
| 45 | +% --- Things that don't --- |
| 46 | +MGLEVEL= 0 % NK replaces MG |
| 47 | +LINEAR_SOLVER= FGMRES % It will be FGMRES regardless |
| 48 | + |
| 49 | +% -------------------- COMPRESSIBLE FREE-STREAM DEFINITION --------------------% |
| 50 | +% |
| 51 | +MACH_NUMBER= 0.8395 |
| 52 | +AOA= 3.06 |
| 53 | +SIDESLIP_ANGLE= 0.0 |
| 54 | + |
| 55 | +FREESTREAM_TEMPERATURE= 288.15 |
| 56 | +REYNOLDS_NUMBER= 11.72E6 |
| 57 | +REYNOLDS_LENGTH= 0.64607 |
| 58 | + |
| 59 | +% ---- IDEAL GAS, POLYTROPIC, VAN DER WAALS AND PENG ROBINSON CONSTANTS -------% |
| 60 | +% |
| 61 | +FLUID_MODEL= STANDARD_AIR |
| 62 | +GAMMA_VALUE= 1.4 |
| 63 | +GAS_CONSTANT= 287.058 |
| 64 | +ACENTRIC_FACTOR= 0.035 |
| 65 | + |
| 66 | +% --------------------------- VISCOSITY MODEL ---------------------------------% |
| 67 | +% |
| 68 | +VISCOSITY_MODEL= SUTHERLAND |
| 69 | +MU_CONSTANT= 1.716E-5 |
| 70 | +MU_REF= 1.716E-5 |
| 71 | +MU_T_REF= 273.15 |
| 72 | +SUTHERLAND_CONSTANT= 110.4 |
| 73 | + |
| 74 | +% ---------------------- REFERENCE VALUE DEFINITION ---------------------------% |
| 75 | +% |
| 76 | +REF_ORIGIN_MOMENT_X = 0.25 |
| 77 | +REF_ORIGIN_MOMENT_Y = 0.00 |
| 78 | +REF_ORIGIN_MOMENT_Z = 0.00 |
| 79 | +REF_LENGTH= 0.64607 |
| 80 | +REF_AREA= 0 |
| 81 | + |
| 82 | +% -------------------- BOUNDARY CONDITION DEFINITION --------------------------% |
| 83 | +% |
| 84 | +MARKER_HEATFLUX= ( WING, 0.0 ) |
| 85 | +MARKER_FAR= ( FARFIELD ) |
| 86 | +MARKER_SYM= ( SYMMETRY ) |
| 87 | +MARKER_PLOTTING= ( WING ) |
| 88 | +MARKER_MONITORING= ( WING ) |
| 89 | + |
| 90 | +% -------------------- FLOW NUMERICAL METHOD DEFINITION -----------------------% |
| 91 | +% |
| 92 | +NUM_METHOD_GRAD= GREEN_GAUSS |
| 93 | +CONV_NUM_METHOD_FLOW= ROE |
| 94 | +MUSCL_FLOW= YES |
| 95 | +SLOPE_LIMITER_FLOW= VAN_ALBADA_EDGE |
| 96 | + |
| 97 | +% -------------------- TURBULENT NUMERICAL METHOD DEFINITION ------------------% |
| 98 | +% |
| 99 | +CONV_NUM_METHOD_TURB= SCALAR_UPWIND |
| 100 | +MUSCL_TURB= NO |
| 101 | +TIME_DISCRE_TURB= EULER_IMPLICIT |
| 102 | + |
| 103 | +% --------------------------- CONVERGENCE PARAMETERS --------------------------% |
| 104 | +% |
| 105 | +CONV_CRITERIA= RESIDUAL |
| 106 | +CONV_RESIDUAL_MINVAL= -11 |
| 107 | +CONV_STARTITER= 10 |
| 108 | +ITER= 2000 |
| 109 | + |
| 110 | +% ------------------------- INPUT/OUTPUT INFORMATION --------------------------% |
| 111 | +% |
| 112 | +MESH_FILENAME= mesh_ONERAM6_turb_hexa_43008.su2 |
| 113 | +MESH_FORMAT= SU2 |
| 114 | +TABULAR_FORMAT= CSV |
| 115 | +SOLUTION_FILENAME= solution.dat |
| 116 | +RESTART_FILENAME= restart.dat |
| 117 | +SOLUTION_ADJ_FILENAME= solution_adj.dat |
| 118 | +RESTART_ADJ_FILENAME= restart_adj.dat |
| 119 | +VOLUME_FILENAME= flow |
| 120 | +VOLUME_ADJ_FILENAME= adjoint |
| 121 | +SURFACE_FILENAME= surface_flow |
| 122 | +SURFACE_ADJ_FILENAME= surface_adjoint |
| 123 | +OUTPUT_FILES=(RESTART, PARAVIEW, SURFACE_PARAVIEW) |
| 124 | +OUTPUT_WRT_FREQ= 10000 |
| 125 | +SCREEN_OUTPUT = (INNER_ITER, WALL_TIME, RMS_DENSITY, RMS_ENERGY, RMS_NU_TILDE, LIFT, DRAG, LINSOL_ITER, LINSOL_RESIDUAL, AVG_CFL) |
| 126 | +CONV_FILENAME= history |
| 127 | + |
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