@@ -30,10 +30,14 @@ CUSTOM_OBJFUNC= outlet_YNO
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% -------------------- FLUID MODEL --------------------------------------- %
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%
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FLUID_MODEL = FLUID_FLAMELET
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+
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+ % List the MLP files describing the respective architectures.
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INTERPOLATION_METHOD = MLP
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- FILENAMES_INTERPOLATOR = (MLP_Group1.mlp, MLP_Group2.mlp, MLP_Group3.mlp, MLP_Group4.mlp, MLP_Group5.mlp, MLP_null.mlp)
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+ FILENAMES_INTERPOLATOR = (MLP_TD1_n.mlp, MLP_TD2.mlp, MLP_PD.mlp, MLP_SPV.mlp, MLP_PNO.mlp, MLP_null.mlp)
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+
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% FGM controlling variable names (must include mixture fraction for partial
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% premixed cases)
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+ PREFERENTIAL_DIFFUSION =YES
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CONTROLLING_VARIABLE_NAMES =(ProgressVariable,EnthalpyTot,MixtureFraction)
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CONTROLLING_VARIABLE_SOURCE_NAMES =(ProdRateTot_PV,NULL,NULL)
@@ -65,17 +69,17 @@ SPECIES_CLIPPING= YES
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SPECIES_CLIPPING_MIN = -1.5064702033996582e+00 -3.4190245000000000e+06 +5.0012799911201000e-03 0
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SPECIES_CLIPPING_MAX = +4.6642374992370605e-01 +2.1569957500000000e+06 +1.4977467060089111e-01 1
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%
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- SPECIES_INIT =(-0.5749236580085463, 2226.901776784524, 0.01446751783896619, 0)
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-
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- MARKER_INLET_SPECIES = (inlet, -0.5749236580085463, 2226.901776784524, 0.01446751783896619, 0)
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- MARKER_INLET =(inlet, 300.0, 0.575,1,0,0)
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+ % Inlet and initial condition corresponding to mixture at T =300K, eq ratio 0.5
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+ SPECIES_INIT =(-0.575, 2.227e3, 1.447e-2, 0)
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+ MARKER_INLET_SPECIES = (inlet, -0.575, 2.227e3, 1.447e-29, 0)
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INC_INLET_TYPE = VELOCITY_INLET
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+ MARKER_INLET =(inlet, 300.0, 0.575,1,0,0)
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CFL_REDUCTION_SPECIES = 1.0
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- MARKER_ISOTHERMAL =(burner_wall, 300 , \
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- cylinder_wall, 300 )
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-
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+ MARKER_ISOTHERMAL =(burner_wall, 350 , \
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+ cylinder_wall, 350 )
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+ MARKER_SPECIES_STRONG_BC =(burner_wall,cylinder_wall)
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MARKER_INTERNAL =(fluid)
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% ---------------------- REFERENCE VALUE DEFINITION ---------------------------%
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%
@@ -100,7 +104,7 @@ MARKER_OUTLET= (outlet, 0.0)
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NUM_METHOD_GRAD = WEIGHTED_LEAST_SQUARES
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CFL_NUMBER = 150
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CFL_ADAPT = NO
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- ITER = 1000
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+ ITER = 3000
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%
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% ------------------------ LINEAR SOLVER DEFINITION ---------------------------%
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%
@@ -116,7 +120,7 @@ MGLEVEL= 0
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% -------------------- FLOW NUMERICAL METHOD DEFINITION -----------------------%
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%
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CONV_NUM_METHOD_FLOW = FDS
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- MUSCL_FLOW = NO
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+ MUSCL_FLOW = YES
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SLOPE_LIMITER_FLOW = NONE
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TIME_DISCRE_FLOW = EULER_IMPLICIT
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%
@@ -126,18 +130,15 @@ CONV_RESIDUAL_MINVAL= -15
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CONV_STARTITER = 10
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CONV_CAUCHY_ELEMS = 100
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CONV_CAUCHY_EPS = 1E-6
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- SCREEN_OUTPUT = INNER_ITER RMS_VELOCITY-X RMS_PRESSURE RMS_ProgressVariable RMS_EnthalpyTot RMS_MixtureFraction CUSTOM
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- %__ADJOINT__SCREEN_OUTPUT = INNER_ITER RMS_ADJ_VELOCITY-X RMS_ADJ_VELOCITY-Y RMS_ADJ_PRESSURE RMS_ADJ_ProgressVariable RMS_ADJ_EnthalpyTot RMS_ADJ_MixtureFraction
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- HISTORY_OUTPUT = RMS_RES CUSTOM
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- %__ADJOINT__HISTORY_OUTPUT = RMS_RES
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+ SCREEN_OUTPUT = INNER_ITER RMS_VELOCITY-X RMS_PRESSURE RMS_ProgressVariable RMS_EnthalpyTot RMS_MixtureFraction
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+ HISTORY_OUTPUT = RMS_RES
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VOLUME_OUTPUT = SOLUTION RESIDUAL SENSITIVITY LOOKUP TIMESTEP PRIMITIVE SOURCE
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CONV_FIELD = RMS_PRESSURE, RMS_VELOCITY-Z, RMS_VELOCITY-Y, RMS_MixtureFraction
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- %__ADJOINT__CONV_FIELD = RMS_ADJ_PRESSURE, RMS_ADJ_VELOCITY-X, RMS_ADJ_VELOCITY-Y, RMS_ADJ_MixtureFraction
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WRT_ZONE_HIST = YES
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%
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% ------------------------- INPUT/OUTPUT INFORMATION --------------------------%
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%
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- RESTART_SOL =YES
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+ RESTART_SOL =NO
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OUTPUT_PRECISION = 16
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TABULAR_FORMAT = CSV
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MESH_FILENAME =H2_burner.su2
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