--- /dev/null
+ObligatoireScalaire=scalar()
+P1=userDiscrete()
+CS_num_FV=modeleNumDuCompo()
+CS_num_CFD_Discrete_Particles=modeleNumDuCompo()
+half_pipe=meshIdentifier()
+inlet=meshGroup()
+outlet=meshGroup()
+wall=meshGroup()
+symetry=meshGroup()
+SD_11=meshGroup()
+inlet1=meshGroup()
+half_pipe2=meshIdentifier()
+Essai=systemGeometry()
+shp1=cadShape()
+time1=simulatedTime()
+Scal1=scalar()
+
+Temporal_Aspects(Simulated_Time_Laps=_F(name=time1,
+ initialTime=0.0,
+ finalTime=2.0,
+ timeDiscretization='Constant Time Step',
+ constantTimeStep=0.1,),);
+
+Spatial_Aspects(System_Geometry=_F(System_Geometry_name=Essai,
+ Shape=_F(Shape_Nature='Typical Geometry',
+ Box='Cube',
+ Size_Of_Bounding_Box=(10.0,10.0,10.0,),
+ ShapeIdentifier=(shp1,),),),
+ Spatial_Discretization=(_F(Mesh_Name=half_pipe,
+ FileFormat='med',
+ FileName='/home/eric/VIMMP/vimmptraining/app/fluide+particule/datafiles/half_pipe.med',
+ GroupIdentifier=(inlet,outlet,wall,symetry,SD_11,),),
+ _F(Mesh_Name=half_pipe2,
+ FileFormat='med',
+ FileName='/home/eric/VIMMP/vimmptraining/app/fluide+particule/datafiles/half_pipe.med',
+ GroupIdentifier=(inlet1,),),),);
+
+FluidComponent=Component(SystemType='Continuum system',
+ PhysicalDescription=_F(FluidComplexe=False,
+ FlowNature='Turbulent',
+ TurbulenceForFlowDynamics=_F(TurbulenceModellingType='One-point moment',
+ RANSModel='Turbulent-Viscosity Model(TVM)',
+ TVMChoice='k-epsilon',),
+ Thermal=_F(ThermalEffects='Non thermal',
+ DensityEquationOfState='Constant density',),
+ Scalars=_F(ScalarsTurbulenceModelling=_F(TurbulenceModellingType='One-point moment',
+ RANSModel=\
+ 'Turbulent-Viscosity Model(TVM)',
+ TVMChoice='k-epsilon',),
+ ImplicitScalar=_F(Name=ObligatoireScalaire,),
+ Scalar=_F(Name=Scal1,),),),
+ NumericalModel=_F(Identifier=CS_num_FV,
+ SimulatedTimeLapse=time1,
+ ModelType='Fields',
+ NumericalMethod='FV',
+ Solver='Code_Saturne',
+ Mesh_Identifiers=(half_pipe,),),);
+
+PartComponent=Component(SystemType='Classical particle system',
+ PhysicalDescription=_F(Particle=_F(ParticleNature='Discrete Particle',
+ DiscreteParticleName=P1,
+ TypeOfDiscreteParticle='Solid',
+ TypeOfSolid='Primary Particle',
+ Properties=_F(Geometry='Sphere',
+ ParticleRadius=99.0,
+ Weight=_F(Mass=99.0,
+ Density=99.0,),
+ Mechanical='Rigid',),
+ List_Of_Interactions=_F(Bonded_Interactions=_F(
+ Type_Of_Bonded_Interaction='No',),
+ Unbonded_Interactions=_F(
+ Type_Of_Unbonded_Interaction='No',),
+ External_Field_Interaction=_F(
+ Type_Of_Interaction_With_An_External_Field='No',),),),),
+ NumericalModel=_F(Identifier=CS_num_CFD_Discrete_Particles,
+ SimulatedTimeLapse=time1,
+ ModelType='Particles',
+ NumericalMethod='CFD_Discrete_Particles',
+ Solver='OpenFOAM',),);
+
+Interactions(Interaction=_F(origine=CS_num_FV,
+ destination=CS_num_CFD_Discrete_Particles,
+ termeLE='Fluid_Velocity_Field',
+ couplingPart=_F(couplingMode='direct',
+ transferType='File',
+ FileFormat='Med',
+ FileName='/home/eric/VIMMP/vimmptraining/app/fluide+particule/datafiles/half_pipe.med',
+ FieldName='velocity',),),);
+#CHECKSUM:533335c85b3d2a04ab411dbc5fdeebe0 -:FIN CHECKSUM
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