--- /dev/null
+Pressure=dynamicVariable()
+Temperature=scalar()
+Time1=simulatedTime()
+CS_Num1=modeleNumDuCompo()
+CS_Num2=modeleNumDuCompo()
+Group_From_Mesh1=meshGroup()
+Group_From_Mesh2=meshGroup()
+Average_Velocity=dynamicVariable()
+Epsilon=scalar()
+outlet=meshGroup()
+symmetry=meshGroup()
+wall=meshGroup()
+inlet1=meshGroup()
+inlet2=meshGroup()
+fluidfile=fileId()
+CS_Num1__CS_Num2_Velocity=interaction()
+CS_Num1__CS_Num2_Epsilon=interaction()
+CS_Num1__CS_Num2_Pressure=interaction()
+Time2=simulatedTime()
+half_pipe_21_60=meshIdentifier()
+half_pipe_15_40=meshIdentifier()
+Interpolated_Pressure_File=fileId()
+Interpolated_Rij_File=fileId()
+Interpolated_Epsilon_File=fileId()
+interpolated_Velocity_File=fileId()
+Position=dynamicVariable()
+Velocity=dynamicVariable()
+Rij=scalar()
+Colloids=userDiscrete()
+Diameter=dynamicVariable()
+Mass=dynamicVariable()
+WallReboundCondition=wallInteractionId()
+FluidSeenVelocity=dynamicVariable()
+CS_Num1__CS_Num2_Rij=interaction()
+
+EnvironementAspects(WorkflowName='Inria',
+ WorkingDirectory='/tmp',);
+
+SpatialAspects(SpatialDiscretization=(_F(MeshId=half_pipe_21_60,
+ MeshName='half_pipe_generation_2inlet',
+ MeshFileFormat='Med',
+ MeshFileName=\
+ '/home/eric/VIMMP/vimmptraining/app/fluide+mapper+particule/datafiles/half_pipe_21_60_2inlet.med',
+ GroupIdentifier=(inlet1,inlet2,outlet,symmetry,wall,Group_From_Mesh1,),),
+ _F(MeshId=half_pipe_15_40,
+ MeshName='half_pipe_generation_2inlet',
+ MeshFileFormat='Med',
+ MeshFileName=\
+ '/home/eric/VIMMP/vimmptraining/app/fluide+mapper+particule/datafiles/half_pipe_15_40_2inlet.med',
+ GroupIdentifier=(inlet1,inlet2,outlet,symmetry,wall,Group_From_Mesh2,),),),);
+
+TemporalAspects(Simulated_Time_Laps=(_F(name=Time1,
+ initialTime=0.0,
+ finalTime=10.0,
+ timeDiscretization='Constant Time Step',
+ constantTimeStep=0.1,),
+ _F(name=Time2,
+ initialTime=10.0,
+ finalTime=15.0,
+ timeDiscretization='Constant Time Step',
+ constantTimeStep=0.01,),),);
+
+FluidComponent=Component(SystemType='Continuum system',
+ PhysicalDescription=_F(ComplexFluid=False,
+ FlowNature='Turbulent',
+ DensityInitialisation=_F(DensityValueType='Value',
+ Density=1.17862,),
+ ViscosityInitialisation=_F(ViscosityValueType='Value',
+ Viscosity=0.0183,),
+ TurbulenceForFlowDynamics=_F(TurbulenceModellingType='One-point moment',
+ RANSModel='Reynolds Stress Model (RSM)',
+ RSMChoice='Rotta',),
+ DynamicalVariables=_F(VariablesSimulation=True,
+ PressureDefinition=_F(Pressure=Pressure,
+ Initialisation=_F(InitialisationType=\
+ 'ByValue',
+ Value=0.0,),
+ SourceTerm=False,),
+ VelocityDefinition=_F(AverageVelocity=Average_Velocity,
+ Initialisation=_F(InitialisationType=\
+ 'ByValue',
+ Value=0.0,),
+ SourceTerm=False,),
+ EpsilonDefinition=_F(Name=Epsilon,
+ Initialisation=_F(InitialisationType=\
+ 'ByValue',
+ Value=1.3e-06,),
+ SourceTerm=False,),
+ RijDefinition=_F(Name=Rij,
+ Initialisation=_F(InitialisationType=\
+ 'ByValue',
+ Value=0.0004,),
+ SourceTerm=False,),),
+ Thermal=_F(ThermalEffects='Non thermal',
+ ReferenceTemperature=293.15,),
+ Scalars=_F(withScalars=False,),),
+ NumericalModel=_F(Identifier=CS_Num1,
+ SimulatedTimeLapse=Time1,
+ ChoiceOfApproach='Field_based',
+ NumericalMethod='FV',
+ Solver='Code_Saturne',
+ MeshIdentifiers=(half_pipe_21_60,),),
+ BoundaryConditions=_F(BoundaryCondition=(_F(TypeOfBoundaryCondition='Inlet',
+ ApplyOnGroups=(inlet1,inlet2,),
+ ApplyOnStateVariable=(Average_Velocity,),
+ FormulationOfBoundary='Dirichlet',
+ Consigne=\
+ 'Choose between InletProfile,IntegratedValue,IntegratedVectorValue ',
+ IntegratedVectorValue=_F(U=1.0,
+ V=0.0,
+ W=0.0,),),
+ _F(TypeOfBoundaryCondition='Outlet',
+ ApplyOnGroups=(outlet,),),
+ _F(TypeOfBoundaryCondition='Wall',
+ ApplyOnGroups=(wall,),
+ VelocityAtBoundary=_F(SlipVelocity=0.0,
+ WallMotion=_F(U=0.0,
+ V=0.0,
+ W=0.0,),),
+ LevelOfDescription=_F(WallFunction='2-scale model (Log law)',),),
+ _F(TypeOfBoundaryCondition='Symmetry',
+ ApplyOnGroups=(symmetry,),
+ ApplyOnStateVariable=(Pressure,Average_Velocity,Epsilon,Rij,),),),),);
+
+PartComponent=Component(SystemType='Classical particle system',
+ PhysicalDescription=_F(Particles=_F(ParticleNature='Discrete Particle',
+ ParticleName=Colloids,
+ InitialNumberOfParticles=0,
+ TypeOfDiscreteParticle='Solid',
+ PrimaryOrAggregate='Primary Particle',
+ Properties=_F(Geometry='Sphere',
+ ReferenceParticleRadius=1e-05,
+ Weight=_F(Density=1000.0,),
+ Mechanical='Rigid',),),
+ AmbiantMediaInteraction=_F(MomentumExchange=_F(withMomentumExchange=True,
+ MomentumFieldType=('Hydrodynamic',),
+ DefineForceOnParticle=_F(
+ TypeOfHydroDynamicForce=('Drag',),
+ FieldAppliesOnAllSpecies=True,
+ NatureOfFluidForce=_F(
+ NatureOfFlow='Turbulent',
+ TurbulenceModellingType='One-point moment',
+ RANSModel='Turbulent-Viscosity Model (TVM)',
+ TurbulenceModelDispersion='Langevin',
+ InitialisationType='ByInteraction',
+ Consigne='Create and choose suitable interaction',
+ InteractionNameForPressure=CS_Num1__CS_Num2_Pressure,
+ InteractionNameForVelocity=CS_Num1__CS_Num2_Velocity,
+ InteractionNameForEpsilon=CS_Num1__CS_Num2_Epsilon,
+ InteractionNameForRij=CS_Num1__CS_Num2_Rij,),),),
+ MassExchange=_F(withMassExchange=False,),
+ EnergyExchange=_F(withEnergyExchange=False,),
+ AmbientInducedProcesses=_F(withAmbientInducedProcesses=\
+ False,),
+ AdditionalSamplingOfAmbientMedia=_F(
+ withAdditionalSamplingOfAmbientMedia=False,),),
+ ParticleParticleInteraction=_F(BondedInteractions=_F(BondedParticles=False,),
+ ActionsAtDistance=_F(withActionsAtDistance=False,),
+ ContactPhenomena=_F(withContactPhenomena=False,),),
+ ParticleWallInteraction=_F(withParticleWallInteraction=True,
+ ParticleWallInteractionId=WallReboundCondition,
+ TypeOfWall=_F(Dynamics='Fixed position',
+ LevelOfDescription='Continuum',
+ SurfaceTexture='Smooth',),
+ ActionsAtDistance=_F(withActionsAtDistance=False,),
+ ContactPhenomena=_F(withContactPhenomena=True,
+ LevelOfDescription='Macroscopic',
+ OutcomeOfContact='Elastic collision',),),
+ ConstraintsAndReducedStatisticalDescription=_F(Constraint=_F(TypeOfConstraint=
+ ('Time-marching_non-equilibrium',
+ ),),),
+ StateVector=_F(ParticleDiameter=_F(Diameter=Diameter,
+ ToSimulate=False,),
+ ParticleMass=_F(Mass=Mass,
+ ToSimulate=False,),
+ ParticlePosition=_F(Position=Position,
+ ToSimulate=True,
+ Initialisation=_F(InitialisationType='Not needed',),),
+ ParticleVelocity=_F(Velocity=Velocity,
+ ToSimulate=True,
+ Initialisation=_F(InitialisationType='Not needed',
+ SourceTerm=False,),),
+ FluidVelocitySeenByParticles=_F(FluidSeenVelocity=FluidSeenVelocity,
+ ToSimulate=True,
+ Initialisation=_F(InitialisationType=\
+ 'Not needed',
+ SourceTerm=False,),),),),
+ NumericalModel=_F(Identifier=CS_Num2,
+ SimulatedTimeLapse=Time2,
+ ChoiceOfApproach='Particle_based',
+ NumericalMethod='CFD_Discrete_Particle_based',
+ Solver='Code_Saturne',
+ MeshIdentifiers=(half_pipe_15_40,),),
+ BoundaryConditions=_F(BoundaryCondition=(_F(TypeOfBoundaryCondition='Inlet',
+ ApplyOnGroups=(inlet2,),
+ NumberOfParticleInjected=100,
+ InjectionEveryNTimeSteps=1,
+ DiameterOfParticleInjected=1e-05,
+ MassOfParticleInjected=4.2e-12,
+ PositionOfParticleInjected=_F(InitialisationMode='ByFormula',),
+ ParticleVelocity=_F(InitialisationMode='ByFormula',),
+ FluidVelocitySeenByParticles=_F(InitialisationMode='ByFormula',),),
+ _F(TypeOfBoundaryCondition='Outlet',
+ ApplyOnGroups=(outlet,inlet1,),),
+ _F(TypeOfBoundaryCondition='Symmetry',
+ ApplyOnGroups=(symmetry,),
+ ApplyOnStateVariable=
+
+ (Position,Velocity,
+ Diameter,Mass,
+ FluidSeenVelocity,),),
+ _F(TypeOfBoundaryCondition='Wall',
+ ApplyOnGroups=(wall,),
+ ApplyOnStateVariable=(Position,Velocity,FluidSeenVelocity,),
+ ChoiceOfParticleWallInteraction=WallReboundCondition,),),),);
+
+MedCouplingComponent=Interpolator(InterpolatorType='Med Coupling',
+ TargetMeshIdentifier=half_pipe_15_40,
+ InterpolationType='P0P0',
+ DefaultValueForUnmatchedMeshTargetEntity=-1.0,);
+
+Interactions(IOAspects=_F(FileTransfer=(_F(TransferId=fluidfile,
+ FileFormat='Med',
+ FileName='results_Fluid_domain.med',),
+ _F(TransferId=interpolated_Velocity_File,
+ FileFormat='Med',
+ FileName='results_Fluid_Interpolated_Velocity.med',),
+ _F(TransferId=Interpolated_Rij_File,
+ FileFormat='Med',
+ FileName='results_Fluid_Interpolated_Rij.med',),
+ _F(TransferId=Interpolated_Epsilon_File,
+ FileFormat='Med',
+ FileName='results_Fluid_Interpolated_Epsilon.med',),
+ _F(TransferId=Interpolated_Pressure_File,
+ FileFormat='Med',
+ FileName='results_Fluid_Interpolated_Pressure.med',),),),
+ Interaction=(_F(InteractionName=CS_Num1__CS_Num2_Velocity,
+ From=CS_Num1,
+ To=CS_Num2,
+ InvolvedStateVariable=Average_Velocity,
+ InteractionConfiguration=_F(OutputId=fluidfile,
+ FieldName='Velocity',
+ CouplingMode='DataProcessing',
+ DataProcessingNode=_F(Tool=MedCouplingComponent,
+ OutputId=interpolated_Velocity_File,
+ FieldName='Velocity',
+ FieldNature='IntensiveMaximum',),),),
+ _F(InteractionName=CS_Num1__CS_Num2_Epsilon,
+ From=CS_Num1,
+ To=CS_Num2,
+ InvolvedStateVariable=Epsilon,
+ InteractionConfiguration=_F(OutputId=fluidfile,
+ FieldName='epsilon',
+ CouplingMode='DataProcessing',
+ DataProcessingNode=_F(Tool=MedCouplingComponent,
+ OutputId=Interpolated_Epsilon_File,
+ FieldName='epsilon',
+ FieldNature='IntensiveMaximum',),),),
+ _F(InteractionName=CS_Num1__CS_Num2_Pressure,
+ From=CS_Num1,
+ To=CS_Num2,
+ InvolvedStateVariable=Pressure,
+ InteractionConfiguration=_F(OutputId=fluidfile,
+ FieldName='Pressure',
+ CouplingMode='DataProcessing',
+ DataProcessingNode=_F(Tool=MedCouplingComponent,
+ OutputId=Interpolated_Pressure_File,
+ FieldName='Pressure',
+ FieldNature='IntensiveMaximum',),),),
+ _F(InteractionName=CS_Num1__CS_Num2_Rij,
+ From=CS_Num1,
+ To=CS_Num2,
+ InvolvedStateVariable=Rij,
+ InteractionConfiguration=_F(OutputId=fluidfile,
+ FieldName='Rij',
+ CouplingMode='DataProcessing',
+ DataProcessingNode=_F(Tool=MedCouplingComponent,
+ OutputId=Interpolated_Rij_File,
+ FieldName='Rij',
+ FieldNature='IntensiveMaximum',),),),),);
+#CHECKSUM:e5f0a89820583811aab53201d988431a -:FIN CHECKSUM
\ No newline at end of file
