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7 | 7 | % File Version 7.3.0 "Blackbird" % |
8 | 8 | % % |
9 | 9 | %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% |
10 | | - |
| 10 | +% |
11 | 11 | % ------------- DIRECT, ADJOINT, AND LINEARIZED PROBLEM DEFINITION ------------% |
12 | 12 | % |
13 | | -% Physical governing equations (EULER, NAVIER_STOKES, |
14 | | -% FEM_EULER, FEM_NAVIER_STOKES, FEM_RANS, FEM_LES, |
15 | | -% WAVE_EQUATION, HEAT_EQUATION, FEM_ELASTICITY, |
16 | | -% POISSON_EQUATION) |
17 | 13 | SOLVER= RANS |
18 | | -% |
19 | | -% Specify turbulence model (NONE, SA, SA_NEG, SST, SA_E, SA_COMP, SA_E_COMP) |
20 | 14 | KIND_TURB_MODEL= SST |
21 | | -% |
22 | | -% Restart solution (NO, YES) |
23 | 15 | RESTART_SOL= YES |
24 | 16 | % |
25 | | -% System of measurements (SI, US) |
26 | | -% International system of units (SI): ( meters, kilograms, Kelvins, |
27 | | -% Newtons = kg m/s^2, Pascals = N/m^2, |
28 | | -% Density = kg/m^3, Speed = m/s, |
29 | | -% Equiv. Area = m^2 ) |
30 | | -% United States customary units (US): ( inches, slug, Rankines, lbf = slug ft/s^2, |
31 | | -% psf = lbf/ft^2, Density = slug/ft^3, |
32 | | -% Speed = ft/s, Equiv. Area = ft^2 ) |
33 | | -SYSTEM_MEASUREMENTS= SI |
34 | | -% |
35 | 17 | AXISYMMETRIC= YES |
36 | 18 | % |
37 | 19 | % -------------------- COMPRESSIBLE FREE-STREAM DEFINITION --------------------% |
38 | 20 | % |
39 | | -% Mach number (non-dimensional, based on the free-stream values) |
40 | 21 | MACH_NUMBER= 1E-9 |
41 | 22 | % |
42 | | -% Angle of attack (degrees, only for compressible flows) |
43 | | -AOA= 0.0 |
44 | | -% |
45 | | -% Side-slip angle (degrees, only for compressible flows) |
46 | | -SIDESLIP_ANGLE= 0.0 |
47 | | -% |
48 | | -% Init option to choose between Reynolds (default) or thermodynamics quantities |
49 | | -% for initializing the solution (REYNOLDS, TD_CONDITIONS) |
50 | 23 | INIT_OPTION= TD_CONDITIONS |
51 | 24 | % |
52 | | -% Free-stream option to choose between density and temperature (default) for |
53 | | -% initializing the solution (TEMPERATURE_FS, DENSITY_FS) |
54 | 25 | FREESTREAM_OPTION= TEMPERATURE_FS |
55 | | -% |
56 | | -% Free-stream pressure (101325.0 N/m^2, 2116.216 psf by default) |
57 | 26 | FREESTREAM_PRESSURE= 1400000 |
58 | | -% |
59 | | -% Free-stream temperature (288.15 K, 518.67 R by default) |
60 | 27 | FREESTREAM_TEMPERATURE= 373.15 |
61 | 28 | % |
62 | | -% Compressible flow non-dimensionalization (DIMENSIONAL, FREESTREAM_PRESS_EQ_ONE, |
63 | | -% FREESTREAM_VEL_EQ_MACH, FREESTREAM_VEL_EQ_ONE) |
64 | 29 | REF_DIMENSIONALIZATION= DIMENSIONAL |
65 | | - |
| 30 | +% |
66 | 31 | % ---- IDEAL GAS, POLYTROPIC, VAN DER WAALS AND PENG ROBINSON CONSTANTS -------% |
67 | 32 | % |
68 | | -% Fluid model (STANDARD_AIR, IDEAL_GAS, VW_GAS, PR_GAS, |
69 | | -% CONSTANT_DENSITY, INC_IDEAL_GAS, INC_IDEAL_GAS_POLY) |
70 | 33 | FLUID_MODEL= STANDARD_AIR |
71 | | - |
| 34 | +% |
72 | 35 | % --------------------------- VISCOSITY MODEL ---------------------------------% |
73 | 36 | % |
74 | | -% Viscosity model (SUTHERLAND, CONSTANT_VISCOSITY, POLYNOMIAL_VISCOSITY). |
75 | 37 | VISCOSITY_MODEL= CONSTANT_VISCOSITY |
| 38 | +MU_CONSTANT= 1.716E-5 |
76 | 39 | % |
77 | | -% Molecular Viscosity that would be constant (1.716E-5 by default) |
78 | | -MU_CONSTANT= 1.716E-5 |
79 | | - |
80 | 40 | % --------------------------- THERMAL CONDUCTIVITY MODEL ----------------------% |
81 | 41 | % |
82 | | -% Laminar Conductivity model (CONSTANT_CONDUCTIVITY, CONSTANT_PRANDTL, |
83 | | -% POLYNOMIAL_CONDUCTIVITY). |
84 | 42 | CONDUCTIVITY_MODEL= CONSTANT_PRANDTL |
85 | | -% |
86 | | -% Laminar Prandtl number (0.72 (air), only for CONSTANT_PRANDTL) |
87 | 43 | PRANDTL_LAM= 0.72 |
88 | | -% |
89 | | -% Turbulent Prandtl number (0.9 (air) by default) |
90 | 44 | PRANDTL_TURB= 0.90 |
91 | | - |
| 45 | +% |
92 | 46 | % -------------------- BOUNDARY CONDITION DEFINITION --------------------------% |
93 | 47 | % |
94 | | -% Navier-Stokes (no-slip), constant heat flux wall marker(s) (NONE = no marker) |
95 | | -% Format: ( marker name, constant heat flux (J/m^2), ... ) |
96 | 48 | MARKER_HEATFLUX= ( WALL, 0.0 ) |
97 | | -% |
98 | | -% Symmetry boundary marker(s) (NONE = no marker) |
99 | 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 ) |
100 | 52 | % |
101 | | -% Riemann boundary marker(s) (NONE = no marker) |
102 | | -% Format: (marker, data kind flag, list of data) |
103 | | -MARKER_RIEMANN= ( INFLOW, TOTAL_CONDITIONS_PT, 1400000.0, 373.15, 1.0, 0.0, 0.0, OUTFLOW, STATIC_PRESSURE, 100000.0, 0.0, 0.0, 0.0, 0.0 ) |
104 | | - |
105 | 53 | % ------------- COMMON PARAMETERS DEFINING THE NUMERICAL METHOD ---------------% |
106 | 54 | % |
107 | | -% Numerical method for spatial gradients (GREEN_GAUSS, WEIGHTED_LEAST_SQUARES) |
108 | 55 | NUM_METHOD_GRAD= GREEN_GAUSS |
109 | 56 | % |
110 | | -% CFL number (initial value for the adaptive CFL number) |
111 | 57 | CFL_NUMBER= 1000.0 |
112 | | -% |
113 | | -% Adaptive CFL number (NO, YES) |
114 | 58 | CFL_ADAPT= NO |
115 | | -% |
116 | | -% Parameters of the adaptive CFL number (factor down, factor up, CFL min value, |
117 | | -% CFL max value ) |
118 | | -CFL_ADAPT_PARAM= ( 0.1, 2.0, 10.0, 1000.0 ) |
119 | | -% |
120 | | -% Maximum Delta Time in local time stepping simulations |
121 | 59 | MAX_DELTA_TIME= 1E6 |
122 | | - |
| 60 | +% |
123 | 61 | % ----------- SLOPE LIMITER AND DISSIPATION SENSOR DEFINITION -----------------% |
124 | 62 | % |
125 | | -% Monotonic Upwind Scheme for Conservation Laws (TVD) in the flow equations. |
126 | | -% Required for 2nd order upwind schemes (NO, YES) |
127 | 63 | MUSCL_FLOW= YES |
128 | | -% |
129 | | -% Slope limiter (NONE, VENKATAKRISHNAN, VENKATAKRISHNAN_WANG, |
130 | | -% BARTH_JESPERSEN, VAN_ALBADA_EDGE) |
131 | 64 | SLOPE_LIMITER_FLOW= NONE |
132 | | - |
| 65 | +% |
133 | 66 | % ------------------------ LINEAR SOLVER DEFINITION ---------------------------% |
134 | 67 | % |
135 | | -% Linear solver or smoother for implicit formulations (BCGSTAB, FGMRES, SMOOTHER_JACOBI, |
136 | | -% SMOOTHER_ILU, SMOOTHER_LUSGS, |
137 | | -% SMOOTHER_LINELET) |
138 | 68 | LINEAR_SOLVER= FGMRES |
139 | | -% |
140 | | -% Preconditioner of the Krylov linear solver (ILU, LU_SGS, LINELET, JACOBI) |
141 | 69 | LINEAR_SOLVER_PREC= ILU |
142 | | -% |
143 | | -% Linear solver ILU preconditioner fill-in level (0 by default) |
144 | 70 | LINEAR_SOLVER_ILU_FILL_IN= 0 |
145 | | -% |
146 | | -% Minimum error of the linear solver for implicit formulations |
147 | 71 | LINEAR_SOLVER_ERROR= 0.01 |
148 | | -% |
149 | | -% Max number of iterations of the linear solver for the implicit formulation |
150 | 72 | LINEAR_SOLVER_ITER= 10 |
151 | | - |
| 73 | +% |
152 | 74 | % -------------------------- MULTIGRID PARAMETERS -----------------------------% |
153 | 75 | % |
154 | | -% Multi-grid levels (0 = no multi-grid) |
155 | 76 | MGLEVEL= 0 |
156 | | - |
| 77 | +% |
157 | 78 | % -------------------- FLOW NUMERICAL METHOD DEFINITION -----------------------% |
158 | 79 | % |
159 | | -% Convective numerical method (JST, LAX-FRIEDRICH, CUSP, ROE, AUSM, AUSMPLUSUP, AUSMPLUSUP2, HLLC, |
160 | | -% TURKEL_PREC, MSW, FDS) |
161 | 80 | CONV_NUM_METHOD_FLOW= ROE |
162 | | -% |
163 | | -% Entropy fix coefficient (0.0 implies no entropy fixing, 1.0 implies scalar |
164 | | -% artificial dissipation) |
165 | 81 | ENTROPY_FIX_COEFF= 0.1 |
166 | | -% |
167 | | -% Time discretization (RUNGE-KUTTA_EXPLICIT, EULER_IMPLICIT, EULER_EXPLICIT) |
168 | 82 | TIME_DISCRE_FLOW= EULER_IMPLICIT |
169 | 83 | % |
170 | | - |
171 | 84 | % -------------------- TURBULENT NUMERICAL METHOD DEFINITION ------------------% |
172 | 85 | % |
173 | | -% Convective numerical method (SCALAR_UPWIND) |
174 | 86 | CONV_NUM_METHOD_TURB= SCALAR_UPWIND |
175 | | -% |
176 | | -% Time discretization (EULER_IMPLICIT) |
177 | 87 | TIME_DISCRE_TURB= EULER_IMPLICIT |
178 | | -% |
179 | | -% Reduction factor of the CFL coefficient in the turbulence problem |
180 | 88 | CFL_REDUCTION_TURB= 1.0 |
181 | | - |
| 89 | +% |
182 | 90 | % --------------------------- CONVERGENCE PARAMETERS --------------------------% |
183 | 91 | % |
184 | | -% Number of total iterations |
185 | 92 | ITER= 1000 |
186 | | -% |
187 | | -% Min value of the residual (log10 of the residual) |
188 | 93 | CONV_RESIDUAL_MINVAL= -12 |
189 | | -% |
190 | | -% Start convergence criteria at iteration number |
191 | 94 | CONV_STARTITER= 10 |
192 | | - |
| 95 | +% |
193 | 96 | % ------------------------- INPUT/OUTPUT INFORMATION --------------------------% |
194 | 97 | % |
195 | | -% Mesh input file |
196 | 98 | MESH_FILENAME= nozzle.su2 |
197 | 99 | % |
198 | | -% Mesh input file format (SU2, CGNS) |
199 | | -MESH_FORMAT= SU2 |
200 | | -% |
201 | | -% Restart flow input file |
202 | 100 | SOLUTION_FILENAME= solution_flow.dat |
203 | | -% |
204 | | -% Writing solution file frequency |
205 | 101 | OUTPUT_WRT_FREQ= 1000 |
206 | 102 | % |
207 | | -% Screen output |
208 | | -SCREEN_OUTPUT= (INNER_ITER, RMS_DENSITY, RMS_ENERGY, RMS_TKE, RMS_DISSIPATION, RMS_ADJ_DENSITY, RMS_ADJ_ENERGY, RMS_ADJ_TKE, RMS_ADJ_DISSIPATION) |
| 103 | +% Note: This cfg is used for a primal and adjoint Testcase, therefore both residuals are present here. |
| 104 | +SCREEN_OUTPUT= (INNER_ITER, RMS_DENSITY, RMS_ENERGY, RMS_TKE, RMS_DISSIPATION, \ |
| 105 | + RMS_ADJ_DENSITY, RMS_ADJ_ENERGY, RMS_ADJ_TKE, RMS_ADJ_DISSIPATION) |
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