|
| 1 | +% ------------------------------- SOLVER -------------------------------- % |
| 2 | +% |
| 3 | +SOLVER= RANS |
| 4 | +KIND_TURB_MODEL= SA |
| 5 | +REF_DIMENSIONALIZATION= FREESTREAM_VEL_EQ_MACH |
| 6 | +% |
| 7 | +% ----------------------------- FREESTREAM ------------------------------ % |
| 8 | +% |
| 9 | +MACH_NUMBER= 0.17 |
| 10 | +AOA= 5.5 |
| 11 | +INIT_OPTION= REYNOLDS |
| 12 | +FREESTREAM_OPTION= TEMPERATURE_FS |
| 13 | +FREESTREAM_TEMPERATURE= 295.56 |
| 14 | +REYNOLDS_NUMBER= 1.71E6 |
| 15 | +REYNOLDS_LENGTH= 0.4572 |
| 16 | +% |
| 17 | +% -------------------------- REFERENCE VALUES --------------------------- % |
| 18 | +% |
| 19 | +REF_AREA= 0.4572 |
| 20 | +REF_LENGTH= 0.4572 |
| 21 | +REF_ORIGIN_MOMENT_X= 0.0 |
| 22 | +REF_ORIGIN_MOMENT_Y= 0.0 |
| 23 | +REF_ORIGIN_MOMENT_Z= 0.0 |
| 24 | +% |
| 25 | +% ------------------------- BOUNDARY CONDITIONS ------------------------- % |
| 26 | +% |
| 27 | +MARKER_HEATFLUX= ( wall, 0.0 ) |
| 28 | +MARKER_FAR= ( farfield ) |
| 29 | +MARKER_PLOTTING= ( wall ) |
| 30 | +MARKER_MONITORING= ( wall ) |
| 31 | +% |
| 32 | +% ---------------------------- FLUID MODELS ----------------------------- % |
| 33 | +% |
| 34 | +FLUID_MODEL= STANDARD_AIR |
| 35 | +GAMMA_VALUE= 1.4 |
| 36 | +GAS_CONSTANT= 287.058 |
| 37 | +% |
| 38 | +VISCOSITY_MODEL= SUTHERLAND |
| 39 | +MU_REF= 1.716E-5 |
| 40 | +MU_T_REF= 273.15 |
| 41 | +SUTHERLAND_CONSTANT= 110.4 |
| 42 | +% |
| 43 | +CONDUCTIVITY_MODEL= CONSTANT_PRANDTL |
| 44 | +PRANDTL_LAM= 0.72 |
| 45 | +PRANDTL_TURB= 0.90 |
| 46 | +% |
| 47 | +% ----------------------- SPATIAL DISCRETIZATION ------------------------ % |
| 48 | +% |
| 49 | +NUM_METHOD_GRAD= GREEN_GAUSS |
| 50 | +CONV_NUM_METHOD_FLOW= ROE |
| 51 | +ENTROPY_FIX_COEFF= 1e-5 |
| 52 | +MUSCL_FLOW= YES |
| 53 | +SLOPE_LIMITER_FLOW= VAN_ALBADA_EDGE |
| 54 | +% |
| 55 | +CONV_NUM_METHOD_TURB= SCALAR_UPWIND |
| 56 | +MUSCL_TURB= NO |
| 57 | +% |
| 58 | +% ---------- PSEUDOTIME INTEGRATION / CONVERGENCE ACCELERATION ---------- % |
| 59 | +% |
| 60 | +USE_VECTORIZATION= YES |
| 61 | +TIME_DISCRE_FLOW= EULER_IMPLICIT |
| 62 | +TIME_DISCRE_TURB= EULER_IMPLICIT |
| 63 | +% |
| 64 | +CFL_NUMBER= 40 |
| 65 | +CFL_REDUCTION_TURB= 1.0 |
| 66 | +CFL_ADAPT= NO |
| 67 | +% |
| 68 | +LINEAR_SOLVER= FGMRES |
| 69 | +LINEAR_SOLVER_PREC= ILU |
| 70 | +LINEAR_SOLVER_ERROR= 0.2 |
| 71 | +LINEAR_SOLVER_ITER= 4 |
| 72 | +% |
| 73 | +MGLEVEL= 0 |
| 74 | +NEWTON_KRYLOV= YES |
| 75 | +NEWTON_KRYLOV_IPARAM= ( 0, 0, 1 ) % n0, np, ft |
| 76 | +NEWTON_KRYLOV_DPARAM= ( 0.0, 1e-20, -3, 1e-5 ) % r0, tp, rf, e |
| 77 | +% |
| 78 | +% ------------------------ CONVERGENCE CRITERIA ------------------------- % |
| 79 | +% |
| 80 | +ITER= 10000 |
| 81 | +CONV_RESIDUAL_MINVAL= -11.5 |
| 82 | +% |
| 83 | +% --------------------------- INPUT / OUTPUT ---------------------------- % |
| 84 | +% |
| 85 | +MESH_FILENAME= 2D_L1_coarse_r1.su2 |
| 86 | +MESH_FORMAT= SU2 |
| 87 | +RESTART_SOL= YES |
| 88 | +OUTPUT_WRT_FREQ= 1000 |
| 89 | +SCREEN_WRT_FREQ_INNER= 1 |
| 90 | +HISTORY_OUTPUT= ( ITER, RMS_RES, AERO_COEFF ) |
| 91 | +SCREEN_OUTPUT= ( INNER_ITER, RMS_DENSITY, RMS_MOMENTUM-X, RMS_MOMENTUM-Y,\ |
| 92 | + RMS_ENERGY, RMS_NU_TILDE, DRAG, LIFT, MOMENT_Z,\ |
| 93 | + LINSOL_RESIDUAL ) |
| 94 | + |
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