The new flexible and extensible modular solvers structure already provides most
of the simulation functionality needed for single phase, multiphase,
multicomponent etc. fluid flow problems as well as a very effective method of
combining these with solid heat transfer, solid stress, surface film to solve
complex multi-region, multi-physics problems and are now the primary mechanism
for the further development of OpenFOAM simulation capability in future. To
emphasis this for both users and developers the applications/solvers directory
has been separated into applications/modules containing all the solver modules:
├── modules
│ ├── compressibleMultiphaseVoF
│ ├── compressibleVoF
│ ├── film
│ ├── fluid
│ ├── fluidSolver
│ ├── functions
│ ├── incompressibleDenseParticleFluid
│ ├── incompressibleDriftFlux
│ ├── incompressibleFluid
│ ├── incompressibleMultiphaseVoF
│ ├── incompressibleVoF
│ ├── isothermalFilm
│ ├── isothermalFluid
│ ├── movingMesh
│ ├── multicomponentFluid
│ ├── multiphaseEuler
│ ├── multiphaseVoFSolver
│ ├── shockFluid
│ ├── solid
│ ├── solidDisplacement
│ ├── twoPhaseSolver
│ ├── twoPhaseVoFSolver
│ ├── VoFSolver
│ └── XiFluid
applications/solvers containing the foamRun and foamMultiRun solver applications
which instantiate and execute the chosen solver modules and also standalone
solver applications for special initialisation and test activities:
├── solvers
│ ├── boundaryFoam
│ ├── chemFoam
│ ├── foamMultiRun
│ ├── foamRun
│ └── potentialFoam
and applications/legacy containing legacy solver applications which are not
currently being actively developed but the functionality of which will be merged
into the solver modules or form the basis of new solver modules as the need
arises:
├── legacy
│ ├── basic
│ │ ├── financialFoam
│ │ └── laplacianFoam
│ ├── combustion
│ │ └── PDRFoam
│ ├── compressible
│ │ └── rhoPorousSimpleFoam
│ ├── electromagnetics
│ │ ├── electrostaticFoam
│ │ ├── magneticFoam
│ │ └── mhdFoam
│ ├── incompressible
│ │ ├── adjointShapeOptimisationFoam
│ │ ├── dnsFoam
│ │ ├── icoFoam
│ │ ├── porousSimpleFoam
│ │ └── shallowWaterFoam
│ └── lagrangian
│ ├── dsmcFoam
│ ├── mdEquilibrationFoam
│ └── mdFoam
Correspondingly the tutorials directory structure has been reorganised with the
modular solver directories at the top level with names that make it easier for
users to find example cases relating to their particular requirements and a
legacy sub-directory containing cases corresponding to the legacy solver
applications listed above:
├── compressibleMultiphaseVoF
│ └── damBreak4phaseLaminar
├── compressibleVoF
│ ├── ballValve
│ ├── climbingRod
│ ├── damBreak
│ ├── depthCharge2D
│ ├── depthCharge3D
│ ├── sloshingTank2D
│ └── throttle
├── film
│ └── rivuletPanel
├── fluid
│ ├── aerofoilNACA0012
│ ├── aerofoilNACA0012Steady
│ ├── angledDuct
│ ├── angledDuctExplicitFixedCoeff
│ ├── angledDuctLTS
│ ├── annularThermalMixer
│ ├── BernardCells
│ ├── blockedChannel
│ ├── buoyantCavity
│ ├── cavity
│ ├── decompressionTank
│ ├── externalCoupledCavity
│ ├── forwardStep
│ ├── helmholtzResonance
│ ├── hotRadiationRoom
│ ├── hotRadiationRoomFvDOM
│ ├── hotRoom
│ ├── hotRoomBoussinesq
│ ├── hotRoomBoussinesqSteady
│ ├── hotRoomComfort
│ ├── iglooWithFridges
│ ├── mixerVessel2DMRF
│ ├── nacaAirfoil
│ ├── pitzDaily
│ ├── prism
│ ├── shockTube
│ ├── squareBend
│ ├── squareBendLiq
│ └── squareBendLiqSteady
├── incompressibleDenseParticleFluid
│ ├── column
│ ├── cyclone
│ ├── Goldschmidt
│ ├── GoldschmidtMPPIC
│ └── injectionChannel
├── incompressibleDriftFlux
│ ├── dahl
│ ├── mixerVessel2DMRF
│ └── tank3D
├── incompressibleFluid
│ ├── airFoil2D
│ ├── ballValve
│ ├── blockedChannel
│ ├── cavity
│ ├── cavityCoupledU
│ ├── channel395
│ ├── drivaerFastback
│ ├── ductSecondaryFlow
│ ├── elipsekkLOmega
│ ├── flowWithOpenBoundary
│ ├── hopperParticles
│ ├── impeller
│ ├── mixerSRF
│ ├── mixerVessel2D
│ ├── mixerVessel2DMRF
│ ├── mixerVesselHorizontal2DParticles
│ ├── motorBike
│ ├── motorBikeSteady
│ ├── movingCone
│ ├── offsetCylinder
│ ├── oscillatingInlet
│ ├── pipeCyclic
│ ├── pitzDaily
│ ├── pitzDailyLES
│ ├── pitzDailyLESDevelopedInlet
│ ├── pitzDailyLTS
│ ├── pitzDailyPulse
│ ├── pitzDailyScalarTransport
│ ├── pitzDailySteady
│ ├── pitzDailySteadyExperimentalInlet
│ ├── pitzDailySteadyMappedToPart
│ ├── pitzDailySteadyMappedToRefined
│ ├── planarContraction
│ ├── planarCouette
│ ├── planarPoiseuille
│ ├── porousBlockage
│ ├── propeller
│ ├── roomResidenceTime
│ ├── rotor2DRotating
│ ├── rotor2DSRF
│ ├── rotorDisk
│ ├── T3A
│ ├── TJunction
│ ├── TJunctionFan
│ ├── turbineSiting
│ ├── waveSubSurface
│ ├── windAroundBuildings
│ └── wingMotion
├── incompressibleMultiphaseVoF
│ ├── damBreak4phase
│ ├── damBreak4phaseFineLaminar
│ ├── damBreak4phaseLaminar
│ └── mixerVessel2DMRF
├── incompressibleVoF
│ ├── angledDuct
│ ├── capillaryRise
│ ├── cavitatingBullet
│ ├── climbingRod
│ ├── containerDischarge2D
│ ├── damBreak
│ ├── damBreakLaminar
│ ├── damBreakPorousBaffle
│ ├── damBreakWithObstacle
│ ├── DTCHull
│ ├── DTCHullMoving
│ ├── DTCHullWave
│ ├── floatingObject
│ ├── floatingObjectWaves
│ ├── forcedUpstreamWave
│ ├── mixerVessel
│ ├── mixerVessel2DMRF
│ ├── mixerVesselHorizontal2D
│ ├── nozzleFlow2D
│ ├── planingHullW3
│ ├── propeller
│ ├── sloshingCylinder
│ ├── sloshingTank2D
│ ├── sloshingTank2D3DoF
│ ├── sloshingTank3D
│ ├── sloshingTank3D3DoF
│ ├── sloshingTank3D6DoF
│ ├── testTubeMixer
│ ├── waterChannel
│ ├── wave
│ ├── wave3D
│ └── weirOverflow
├── isothermalFilm
│ └── rivuletPanel
├── isothermalFluid
│ ├── potentialFreeSurfaceMovingOscillatingBox
│ └── potentialFreeSurfaceOscillatingBox
├── legacy
│ ├── basic
│ │ ├── financialFoam
│ │ │ └── europeanCall
│ │ └── laplacianFoam
│ │ └── flange
│ ├── combustion
│ │ └── PDRFoam
│ │ └── flamePropagationWithObstacles
│ ├── compressible
│ │ └── rhoPorousSimpleFoam
│ │ ├── angledDuctExplicit
│ │ └── angledDuctImplicit
│ ├── electromagnetics
│ │ ├── electrostaticFoam
│ │ │ └── chargedWire
│ │ └── mhdFoam
│ │ └── hartmann
│ ├── incompressible
│ │ ├── adjointShapeOptimisationFoam
│ │ │ └── pitzDaily
│ │ ├── dnsFoam
│ │ │ └── boxTurb16
│ │ ├── icoFoam
│ │ │ ├── cavity
│ │ │ └── elbow
│ │ ├── porousSimpleFoam
│ │ │ ├── angledDuctExplicit
│ │ │ └── angledDuctImplicit
│ │ └── shallowWaterFoam
│ │ └── squareBump
│ ├── lagrangian
│ │ ├── dsmcFoam
│ │ │ ├── freeSpacePeriodic
│ │ │ ├── freeSpaceStream
│ │ │ ├── supersonicCorner
│ │ │ └── wedge15Ma5
│ │ ├── mdEquilibrationFoam
│ │ │ ├── periodicCubeArgon
│ │ │ └── periodicCubeWater
│ │ └── mdFoam
│ │ └── nanoNozzle
├── mesh
│ ├── blockMesh
│ │ ├── pipe
│ │ ├── sphere
│ │ ├── sphere7
│ │ └── sphere7ProjectedEdges
│ ├── refineMesh
│ │ └── refineFieldDirs
│ └── snappyHexMesh
│ ├── flange
│ └── pipe
├── movingMesh
│ └── SnakeRiverCanyon
├── multicomponentFluid
│ ├── aachenBomb
│ ├── counterFlowFlame2D
│ ├── counterFlowFlame2D_GRI
│ ├── counterFlowFlame2D_GRI_TDAC
│ ├── counterFlowFlame2DLTS
│ ├── counterFlowFlame2DLTS_GRI_TDAC
│ ├── DLR_A_LTS
│ ├── filter
│ ├── lockExchange
│ ├── membrane
│ ├── nc7h16
│ ├── parcelInBox
│ ├── SandiaD_LTS
│ ├── simplifiedSiwek
│ ├── smallPoolFire2D
│ ├── smallPoolFire3D
│ ├── verticalChannel
│ ├── verticalChannelLTS
│ └── verticalChannelSteady
├── multiphaseEuler
│ ├── bed
│ ├── bubbleColumn
│ ├── bubbleColumnEvaporating
│ ├── bubbleColumnEvaporatingDissolving
│ ├── bubbleColumnEvaporatingReacting
│ ├── bubbleColumnIATE
│ ├── bubbleColumnLaminar
│ ├── bubbleColumnLES
│ ├── bubblePipe
│ ├── damBreak4phase
│ ├── fluidisedBed
│ ├── fluidisedBedLaminar
│ ├── Grossetete
│ ├── hydrofoil
│ ├── injection
│ ├── LBend
│ ├── mixerVessel2D
│ ├── mixerVessel2DMRF
│ ├── pipeBend
│ ├── steamInjection
│ ├── titaniaSynthesis
│ ├── titaniaSynthesisSurface
│ ├── wallBoilingIATE
│ ├── wallBoilingPolydisperse
│ └── wallBoilingPolydisperseTwoGroups
├── multiRegion
│ ├── CHT
│ │ ├── circuitBoardCooling
│ │ ├── coolingCylinder2D
│ │ ├── coolingSphere
│ │ ├── heatedDuct
│ │ ├── heatExchanger
│ │ ├── multiphaseCoolingCylinder2D
│ │ ├── reverseBurner
│ │ ├── shellAndTubeHeatExchanger
│ │ ├── VoFcoolingCylinder2D
│ │ └── wallBoiling
│ └── film
│ ├── cylinder
│ ├── cylinderDripping
│ ├── cylinderVoF
│ ├── hotBoxes
│ ├── rivuletBox
│ ├── rivuletPanel
│ ├── splashPanel
│ └── VoFToFilm
├── potentialFoam
│ ├── cylinder
│ └── pitzDaily
├── resources
│ ├── blockMesh
│ ├── geometry
│ └── thermoData
├── shockFluid
│ ├── biconic25-55Run35
│ ├── forwardStep
│ ├── LadenburgJet60psi
│ ├── movingCone
│ ├── obliqueShock
│ ├── shockTube
│ └── wedge15Ma5
├── solidDisplacement
│ ├── beamEndLoad
│ └── plateHole
└── XiFluid
├── kivaTest
└── moriyoshiHomogeneous
189 lines
5.9 KiB
C++
189 lines
5.9 KiB
C++
/*---------------------------------------------------------------------------*\
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========= |
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
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\\ / O peration | Website: https://openfoam.org
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\\ / A nd | Copyright (C) 2011-2023 OpenFOAM Foundation
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\\/ M anipulation |
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-------------------------------------------------------------------------------
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License
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This file is part of OpenFOAM.
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OpenFOAM is free software: you can redistribute it and/or modify it
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under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 3 of the License, or
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(at your option) any later version.
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OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
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ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
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FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
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for more details.
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You should have received a copy of the GNU General Public License
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along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
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Application
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PDRFoam
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Description
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Solver for compressible premixed/partially-premixed combustion with
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turbulence modelling.
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Combusting RANS code using the b-Xi two-equation model.
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Xi may be obtained by either the solution of the Xi transport
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equation or from an algebraic expression. Both approaches are
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based on Gulder's flame speed correlation which has been shown
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to be appropriate by comparison with the results from the
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spectral model.
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Strain effects are incorporated directly into the Xi equation
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but not in the algebraic approximation. Further work need to be
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done on this issue, particularly regarding the enhanced removal rate
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caused by flame compression. Analysis using results of the spectral
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model will be required.
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For cases involving very lean Propane flames or other flames which are
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very strain-sensitive, a transport equation for the laminar flame
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speed is present. This equation is derived using heuristic arguments
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involving the strain time scale and the strain-rate at extinction.
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the transport velocity is the same as that for the Xi equation.
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For large flames e.g. explosions additional modelling for the flame
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wrinkling due to surface instabilities may be applied.
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PDR (porosity/distributed resistance) modelling is included to handle
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regions containing blockages which cannot be resolved by the mesh.
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The fields used by this solver are:
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betav: Volume porosity
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Lobs: Average diameter of obstacle in cell (m)
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Aw: Obstacle surface area per unit volume (1/m)
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CR: Drag tensor (1/m)
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CT: Turbulence generation parameter (1/m)
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Nv: Number of obstacles in cell per unit volume (m^-2)
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nsv: Tensor whose diagonal indicates the number to subtract from
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Nv to get the number of obstacles crossing the flow in each
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direction.
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\*---------------------------------------------------------------------------*/
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#include "argList.H"
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#include "timeSelector.H"
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#include "psiuMulticomponentThermo.H"
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#include "compressibleMomentumTransportModels.H"
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#include "RASThermophysicalTransportModel.H"
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#include "unityLewisEddyDiffusivity.H"
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#include "laminarFlameSpeed.H"
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#include "XiModel.H"
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#include "PDRDragModel.H"
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#include "ignition.H"
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#include "pimpleControl.H"
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#include "pressureReference.H"
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#include "findRefCell.H"
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#include "constrainPressure.H"
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#include "constrainHbyA.H"
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#include "adjustPhi.H"
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#include "uniformDimensionedFields.H"
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#include "fvModels.H"
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#include "fvConstraints.H"
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#include "fvcDdt.H"
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#include "fvcGrad.H"
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#include "fvcFlux.H"
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#include "fvcReconstruct.H"
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#include "fvcMeshPhi.H"
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#include "fvmDdt.H"
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#include "fvmDiv.H"
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#include "fvmLaplacian.H"
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using namespace Foam;
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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int main(int argc, char *argv[])
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{
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#include "postProcess.H"
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#include "setRootCase.H"
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#include "createTime.H"
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#include "createMesh.H"
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#include "createControl.H"
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#include "readCombustionProperties.H"
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#include "readGravitationalAcceleration.H"
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#include "createFields.H"
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#include "createFieldRefs.H"
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#include "initContinuityErrs.H"
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#include "createTimeControls.H"
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#include "compressibleCourantNo.H"
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#include "setInitialDeltaT.H"
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turbulence->validate();
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scalar StCoNum = 0.0;
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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Info<< "\nStarting time loop\n" << endl;
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while (pimple.run(runTime))
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{
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#include "readTimeControls.H"
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#include "compressibleCourantNo.H"
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#include "setDeltaT.H"
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runTime++;
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Info<< "\n\nTime = " << runTime.name() << endl;
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#include "rhoEqn.H"
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// --- Pressure-velocity PIMPLE corrector loop
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while (pimple.loop())
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{
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fvModels.correct();
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if (pimple.predictTransport())
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{
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turbulence->predict();
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thermophysicalTransport.predict();
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}
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#include "UEqn.H"
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// --- Pressure corrector loop
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while (pimple.correct())
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{
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#include "bEqn.H"
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#include "ftEqn.H"
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#include "EauEqn.H"
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#include "EaEqn.H"
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if (!ign.ignited())
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{
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thermo.heu() == thermo.he();
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}
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#include "pEqn.H"
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}
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if (pimple.correctTransport())
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{
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turbulence->correct();
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thermophysicalTransport.correct();
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}
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}
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runTime.write();
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Info<< "\nExecutionTime = "
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<< runTime.elapsedCpuTime()
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<< " s\n" << endl;
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}
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Info<< "\n end\n";
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return 0;
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}
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// ************************************************************************* //
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