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| 1 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 2 | +% % |
| 3 | +% SU2 configuration file % |
| 4 | +% Case description: Turbulent flow over rough flat plate with zero % |
| 5 | +% pressure gradient % |
| 6 | +% Author: Akshay Koodly % |
| 7 | +% Date: 2020.07.07 % |
| 8 | +% File Version 7.0.x "Blackbird" % |
| 9 | +% % |
| 10 | +%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
| 11 | + |
| 12 | +% ------------- DIRECT, ADJOINT, AND LINEARIZED PROBLEM DEFINITION ------------% |
| 13 | +% |
| 14 | +% Physical governing equations (EULER, NAVIER_STOKES, |
| 15 | +% WAVE_EQUATION, HEAT_EQUATION, FEM_ELASTICITY, |
| 16 | +% POISSON_EQUATION) |
| 17 | +SOLVER= INC_RANS |
| 18 | +% |
| 19 | +% If Navier-Stokes, kind of turbulent model (NONE, SA) |
| 20 | +KIND_TURB_MODEL= SA |
| 21 | + |
| 22 | +% Mathematical problem (DIRECT, CONTINUOUS_ADJOINT) |
| 23 | +MATH_PROBLEM= DIRECT |
| 24 | +% |
| 25 | +% Restart solution (NO, YES) |
| 26 | +RESTART_SOL= NO |
| 27 | +% |
| 28 | +% ---------------- INCOMPRESSIBLE FLOW CONDITION DEFINITION -------------------% |
| 29 | +% |
| 30 | +% Density model within the incompressible flow solver. |
| 31 | +% Options are CONSTANT (default), BOUSSINESQ, or VARIABLE. If VARIABLE, |
| 32 | +% an appropriate fluid model must be selected. |
| 33 | +INC_DENSITY_MODEL= CONSTANT |
| 34 | +% |
| 35 | +% Solve the energy equation in the incompressible flow solver |
| 36 | +INC_ENERGY_EQUATION = NO |
| 37 | +% |
| 38 | +% Initial density for incompressible flows (1.2886 kg/m^3 by default) |
| 39 | +INC_DENSITY_INIT= 1.32905 |
| 40 | +% |
| 41 | +% Initial velocity for incompressible flows (1.0,0,0 m/s by default) |
| 42 | +INC_VELOCITY_INIT= ( 69.4448, 0.0, 0.0 ) |
| 43 | +% |
| 44 | +% Initial temperature for incompressible flows that include the |
| 45 | +% energy equation (288.15 K by default). Value is ignored if |
| 46 | +% INC_ENERGY_EQUATION is false. |
| 47 | +INC_TEMPERATURE_INIT= 300.0 |
| 48 | +% |
| 49 | +% Non-dimensionalization scheme for incompressible flows. Options are |
| 50 | +% INITIAL_VALUES (default), REFERENCE_VALUES, or DIMENSIONAL. |
| 51 | +% INC_*_REF values are ignored unless REFERENCE_VALUES is chosen. |
| 52 | +INC_NONDIM= INITIAL_VALUES |
| 53 | +% |
| 54 | +% Reference density for incompressible flows (1.0 kg/m^3 by default) |
| 55 | +INC_DENSITY_REF= 1.0 |
| 56 | +% |
| 57 | +% Reference velocity for incompressible flows (1.0 m/s by default) |
| 58 | +INC_VELOCITY_REF= 1.0 |
| 59 | +% |
| 60 | +% Reference temperature for incompressible flows that include the |
| 61 | +% energy equation (1.0 K by default) |
| 62 | +INC_TEMPERATURE_REF = 1.0 |
| 63 | +% |
| 64 | +% List of inlet types for incompressible flows. List length must |
| 65 | +% match number of inlet markers. Options: VELOCITY_INLET, PRESSURE_INLET. |
| 66 | +INC_INLET_TYPE= VELOCITY_INLET |
| 67 | + |
| 68 | +% --------------------------- VISCOSITY MODEL ---------------------------------% |
| 69 | +% |
| 70 | +% Viscosity model (SUTHERLAND, CONSTANT_VISCOSITY). |
| 71 | +VISCOSITY_MODEL= CONSTANT_VISCOSITY |
| 72 | +% |
| 73 | +% Molecular Viscosity that would be constant (1.716E-5 by default) |
| 74 | +MU_CONSTANT= 1.84592e-05 |
| 75 | +% |
| 76 | +% Sutherland Viscosity Ref (1.716E-5 default value for AIR SI) |
| 77 | +MU_REF= 1.716E-5 |
| 78 | +% |
| 79 | +% Sutherland Temperature Ref (273.15 K default value for AIR SI) |
| 80 | +MU_T_REF= 273.15 |
| 81 | +% |
| 82 | +% Sutherland constant (110.4 default value for AIR SI) |
| 83 | +SUTHERLAND_CONSTANT= 110.4 |
| 84 | + |
| 85 | +% ---------------------- REFERENCE VALUE DEFINITION ---------------------------% |
| 86 | +% |
| 87 | +% Reference origin for moment computation |
| 88 | +REF_ORIGIN_MOMENT_X = 0.25 |
| 89 | +REF_ORIGIN_MOMENT_Y = 0.00 |
| 90 | +REF_ORIGIN_MOMENT_Z = 0.00 |
| 91 | +% |
| 92 | +% Reference length for pitching, rolling, and yawing non-dimensional moment |
| 93 | +REF_LENGTH= 1.0 |
| 94 | +% |
| 95 | +% Reference area for force coefficients (0 implies automatic calculation) |
| 96 | +REF_AREA= 2.0 |
| 97 | + |
| 98 | +% -------------------- BOUNDARY CONDITION DEFINITION --------------------------% |
| 99 | +% |
| 100 | +% Navier-Stokes wall boundary marker(s) (NONE = no marker) |
| 101 | +MARKER_HEATFLUX= ( wall, 0.0 ) |
| 102 | +%WALL_ROUGHNESS = (wall, 0.000061) |
| 103 | +%WALL_ROUGHNESS = (wall, 0.000123) |
| 104 | +WALL_ROUGHNESS = (wall, 0.000246) |
| 105 | +%WALL_ROUGHNESS = (wall, 0.000984) |
| 106 | +% |
| 107 | +% |
| 108 | +% Inlet boundary marker(s) (NONE = no marker) |
| 109 | +% Format: ( inlet marker, total temperature, total pressure, flow_direction_x, |
| 110 | +% flow_direction_y, flow_direction_z, ... ) |
| 111 | +MARKER_INLET= ( inlet, 300.0, 69.4448, 1.0, 0.0, 0.0 ) |
| 112 | +% |
| 113 | +% Outlet boundary marker(s) (NONE = no marker) |
| 114 | +% Format: ( outlet marker, back pressure, ... ) |
| 115 | +MARKER_OUTLET= ( outlet, 0.0, farfield, 0.0 ) |
| 116 | +% |
| 117 | +INC_OUTLET_TYPE= PRESSURE_OUTLET,PRESSURE_OUTLET |
| 118 | +% |
| 119 | +% Symmetry boundary marker(s) (NONE = no marker) |
| 120 | +MARKER_SYM= ( symmetry ) |
| 121 | +% |
| 122 | +% Marker(s) of the surface to be plotted or designed |
| 123 | +MARKER_PLOTTING= ( wall ) |
| 124 | +% |
| 125 | +% Marker(s) of the surface where the functional (Cd, Cl, etc.) will be evaluated |
| 126 | +MARKER_MONITORING= ( wall ) |
| 127 | + |
| 128 | +% ------------- COMMON PARAMETERS DEFINING THE NUMERICAL METHOD ---------------% |
| 129 | +% |
| 130 | +% Numerical method for spatial gradients (GREEN_GAUSS, LEAST_SQUARES, |
| 131 | +% WEIGHTED_LEAST_SQUARES) |
| 132 | +NUM_METHOD_GRAD= GREEN_GAUSS |
| 133 | +% |
| 134 | +% Courant-Friedrichs-Lewy condition of the finest grid |
| 135 | +CFL_NUMBER= 100.0 |
| 136 | +% |
| 137 | +% Adaptive CFL number (NO, YES) |
| 138 | +CFL_ADAPT= NO |
| 139 | +% |
| 140 | +% Parameters of the adaptive CFL number (factor down, factor up, CFL min value, |
| 141 | +% CFL max value ) |
| 142 | +CFL_ADAPT_PARAM= ( 1.5, 0.5, 1.1, 100.0 ) |
| 143 | +% |
| 144 | +% Runge-Kutta alpha coefficients |
| 145 | +RK_ALPHA_COEFF= ( 0.66667, 0.66667, 1.000000 ) |
| 146 | +% |
| 147 | +% Number of total iterations |
| 148 | +ITER= 1000 |
| 149 | + |
| 150 | +% ------------------------ LINEAR SOLVER DEFINITION ---------------------------% |
| 151 | +% |
| 152 | +% Linear solver for implicit formulations (BCGSTAB, FGMRES) |
| 153 | +LINEAR_SOLVER= FGMRES |
| 154 | +% |
| 155 | +% Preconditioner of the Krylov linear solver (JACOBI, LINELET, LU_SGS) |
| 156 | +LINEAR_SOLVER_PREC= ILU |
| 157 | +% |
| 158 | +% Linael solver ILU preconditioner fill-in level (0 by default) |
| 159 | +LINEAR_SOLVER_ILU_FILL_IN= 0 |
| 160 | +% |
| 161 | +% Minimum error of the linear solver for implicit formulations |
| 162 | +LINEAR_SOLVER_ERROR= 1E-12 |
| 163 | +% |
| 164 | +% Max number of iterations of the linear solver for the implicit formulation |
| 165 | +LINEAR_SOLVER_ITER= 20 |
| 166 | + |
| 167 | +% ----------------------- SLOPE LIMITER DEFINITION ----------------------------% |
| 168 | +% |
| 169 | +% Coefficient for the limiter |
| 170 | +VENKAT_LIMITER_COEFF= 0.1 |
| 171 | +% |
| 172 | +% Coefficient for the sharp edges limiter |
| 173 | +ADJ_SHARP_LIMITER_COEFF= 3.0 |
| 174 | +% |
| 175 | +% Reference coefficient (sensitivity) for detecting sharp edges. |
| 176 | +REF_SHARP_EDGES= 3.0 |
| 177 | +% |
| 178 | +% Remove sharp edges from the sensitivity evaluation (NO, YES) |
| 179 | +SENS_REMOVE_SHARP= NO |
| 180 | + |
| 181 | +% -------------------------- MULTIGRID PARAMETERS -----------------------------% |
| 182 | +% |
| 183 | +% Multi-Grid Levels (0 = no multi-grid) |
| 184 | +MGLEVEL= 0 |
| 185 | +% |
| 186 | +% Multi-grid cycle (V_CYCLE, W_CYCLE, FULLMG_CYCLE) |
| 187 | +MGCYCLE= V_CYCLE |
| 188 | +% |
| 189 | +% Multi-grid pre-smoothing level |
| 190 | +MG_PRE_SMOOTH= ( 1, 1, 1, 1 ) |
| 191 | +% |
| 192 | +% Multi-grid post-smoothing level |
| 193 | +MG_POST_SMOOTH= ( 0, 0, 0, 0 ) |
| 194 | +% |
| 195 | +% Jacobi implicit smoothing of the correction |
| 196 | +MG_CORRECTION_SMOOTH= ( 0, 0, 0, 0 ) |
| 197 | +% |
| 198 | +% Damping factor for the residual restriction |
| 199 | +MG_DAMP_RESTRICTION= 0.8 |
| 200 | +% |
| 201 | +% Damping factor for the correction prolongation |
| 202 | +MG_DAMP_PROLONGATION= 0.8 |
| 203 | + |
| 204 | +% -------------------- FLOW NUMERICAL METHOD DEFINITION -----------------------% |
| 205 | +% |
| 206 | +% Convective numerical method (JST, LAX-FRIEDRICH, CUSP, ROE, AUSM, HLLC, |
| 207 | +% TURKEL_PREC, MSW) |
| 208 | +CONV_NUM_METHOD_FLOW= FDS |
| 209 | +% |
| 210 | +% Monotonic Upwind Scheme for Conservation Laws (TVD) in the flow equations. |
| 211 | +% Required for 2nd order upwind schemes (NO, YES) |
| 212 | +MUSCL_FLOW= YES |
| 213 | +% |
| 214 | +% Slope limiter (NONE, VENKATAKRISHNAN, VENKATAKRISHNAN_WANG, |
| 215 | +% BARTH_JESPERSEN, VAN_ALBADA_EDGE) |
| 216 | +SLOPE_LIMITER_FLOW= NONE |
| 217 | +% |
| 218 | +% 2nd and 4th order artificial dissipation coefficients |
| 219 | +JST_SENSOR_COEFF= ( 0.5, 0.02 ) |
| 220 | +% |
| 221 | +% Time discretization (RUNGE-KUTTA_EXPLICIT, EULER_IMPLICIT, EULER_EXPLICIT) |
| 222 | +TIME_DISCRE_FLOW= EULER_IMPLICIT |
| 223 | + |
| 224 | +% -------------------- TURBULENT NUMERICAL METHOD DEFINITION ------------------% |
| 225 | +% |
| 226 | +% Convective numerical method (SCALAR_UPWIND) |
| 227 | +CONV_NUM_METHOD_TURB= SCALAR_UPWIND |
| 228 | +% |
| 229 | +% Monotonic Upwind Scheme for Conservation Laws (TVD) in the turbulence equations. |
| 230 | +% Required for 2nd order upwind schemes (NO, YES) |
| 231 | +MUSCL_TURB= NO |
| 232 | +% |
| 233 | +% Slope limiter (VENKATAKRISHNAN, MINMOD) |
| 234 | +SLOPE_LIMITER_TURB= VENKATAKRISHNAN |
| 235 | +% |
| 236 | +% Time discretization (EULER_IMPLICIT) |
| 237 | +TIME_DISCRE_TURB= EULER_IMPLICIT |
| 238 | +% --------------------------- CONVERGENCE PARAMETERS --------------------------% |
| 239 | +% |
| 240 | +% Convergence criteria (CAUCHY, RESIDUAL) |
| 241 | +% |
| 242 | +CONV_FIELD= RMS_VELOCITY-X |
| 243 | +% |
| 244 | +% Min value of the residual (log10 of the residual) |
| 245 | +CONV_RESIDUAL_MINVAL= -14 |
| 246 | +% |
| 247 | +% Start convergence criteria at iteration number |
| 248 | +CONV_STARTITER= 10 |
| 249 | + |
| 250 | +% ------------------------- INPUT/OUTPUT INFORMATION --------------------------% |
| 251 | +% |
| 252 | +% Mesh input file |
| 253 | +%MESH_FILENAME= mesh_flatplate_turb_69x49.su2 |
| 254 | +MESH_FILENAME= mesh_flatplate_turb_137x97.su2 |
| 255 | +%MESH_FILENAME= mesh_flatplate_turb_273x193.su2 |
| 256 | +% |
| 257 | +% Mesh input file format (SU2, CGNS, NETCDF_ASCII) |
| 258 | +MESH_FORMAT= SU2 |
| 259 | +% |
| 260 | +% Mesh output file |
| 261 | +MESH_OUT_FILENAME= mesh_out.su2 |
| 262 | +% |
| 263 | +% Restart flow input file |
| 264 | +SOLUTION_FILENAME= restart_flow |
| 265 | +% |
| 266 | +% Output file format (PARAVIEW, TECPLOT, SLT) |
| 267 | +TABULAR_FORMAT= CSV |
| 268 | + |
| 269 | +OUTPUT_FILES= PARAVIEW, RESTART, SURFACE_PARAVIEW |
| 270 | +% |
| 271 | +% Output file convergence history (w/o extension) |
| 272 | +CONV_FILENAME= history |
| 273 | +% |
| 274 | +% Output file restart flow |
| 275 | +RESTART_FILENAME= restart_flow |
| 276 | +% |
| 277 | +% Output file flow (w/o extension) variables |
| 278 | +VOLUME_FILENAME= flow |
| 279 | +% |
| 280 | +% Output file surface flow coefficient (w/o extension) |
| 281 | +SURFACE_FILENAME= surface_flow |
| 282 | +% |
| 283 | +% Writing solution file frequency |
| 284 | +OUTPUT_WRT_FREQ= 100 |
| 285 | +% |
| 286 | +% Writing convergence history frequency |
| 287 | +WRT_CON_FREQ= 1 |
| 288 | +% |
| 289 | +SCREEN_OUTPUT= (WALL_TIME,INNER_ITER, RMS_VELOCITY-X, RMS_NU_TILDE, LIFT,DRAG) |
| 290 | +% |
| 291 | +WRT_FORCES_BREAKDOWN= YES |
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