1212% ------------- DIRECT, ADJOINT, AND LINEARIZED PROBLEM DEFINITION ------------%
1313%
1414SOLVER = INC_RANS
15- %
1615KIND_TURB_MODEL = SST
1716%
1817% ---------------- INCOMPRESSIBLE FLOW CONDITION DEFINITION -------------------%
@@ -50,10 +49,12 @@ PRANDTL_TURB= 0.90
5049KIND_STREAMWISE_PERIODIC = MASSFLOW
5150STREAMWISE_PERIODIC_MASSFLOW = 0.85
5251STREAMWISE_PERIODIC_PRESSURE_DROP = 208.023676
53- INC_OUTLET_DAMPING = 0.0001
52+ INC_OUTLET_DAMPING = 0.01
5453%
5554STREAMWISE_PERIODIC_TEMPERATURE = NO
56- STREAMWISE_PERIODIC_OUTLET_HEAT = -6283.185307
55+ % Computation of outlet heat: Heatflux * Area = Heatflux * pi * radius (as we have an accumulated full circle)
56+ % 5e5[W/m] * pi * 2e-3[m]
57+ STREAMWISE_PERIODIC_OUTLET_HEAT = -3141.5926
5758%
5859% -------------------- BOUNDARY CONDITION DEFINITION --------------------------%
5960%
@@ -78,7 +79,7 @@ MARKER_ANALYZE_AVERAGE = MASSFLUX
7879%
7980% ------------- COMMON PARAMETERS DEFINING THE NUMERICAL METHOD ---------------%
8081%
81- ITER = 3500
82+ ITER = 10000
8283NUM_METHOD_GRAD = GREEN_GAUSS
8384CFL_NUMBER = 1e2
8485%
@@ -108,17 +109,19 @@ TIME_DISCRE_TURB= EULER_IMPLICIT
108109% --------------------------- CONVERGENCE PARAMETERS --------------------------%
109110%
110111CONV_CRITERIA = RESIDUAL
111- CONV_RESIDUAL_MINVAL = -26
112- CONV_STARTITER = 100000000
112+ CONV_FIELD = RMS_TEMPERATURE
113+ CONV_RESIDUAL_MINVAL = -10.9
114+ CONV_STARTITER = 10
113115%
114116% ------------------------- INPUT/OUTPUT INFORMATION --------------------------%
115117%
116118MESH_FILENAME = fluid_FFD.su2
117119%
118120SCREEN_OUTPUT = (INNER_ITER, RMS_PRESSURE, RMS_TEMPERATURE, STREAMWISE_MASSFLOW, STREAMWISE_DP)
119- SCREEN_WRT_FREQ_INNER = 25
121+ SCREEN_WRT_FREQ_INNER = 100
120122%
121123HISTORY_OUTPUT = ( ITER, RMS_RES, STREAMWISE_PERIODIC, FLOW_COEFF, LINSOL, AERO_COEFF )
124+ CONV_FILENAME = history_mfhf
122125%
123126OUTPUT_FILES = ( RESTART, PARAVIEW_MULTIBLOCK )
124127VOLUME_OUTPUT = ( COORDINATES, SOLUTION, RESIDUAL, PRIMITIVE )
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