Commit Graph

22 Commits

Author SHA1 Message Date
e727809bd1 tutorials/multicomponentFluid/aachenBomb: Added Allrun-parallel with load-balancing
to demonstrate multi-constraint load-balancing with both Lagrangian and
chemistry.
2024-06-01 20:46:17 +01:00
40bcabf79f decompositionMethods::parMetis: New interface to the ParMETIS distributor for load-balancing
ParMETIS is a parallel version of METIS and can be used as an alternative to
ptScotch or Zoltan, supporting multi-constraints and redistribution:

Description
    ParMetis redistribution in parallel

    Note: parMetis methods do not support serial operation.

    Parameters
    - Method of decomposition
      - kWay: multilevel k-way
      - geomKway: combined coordinate-based and multi-level k-way
      - adaptiveRepart: balances the work load of a graph

    - Options
      - options[0]: The specified options are used if options[0] = 1

      - options[1]: Specifies the level of information to be returned during
        the execution of the algorithm. Timing information can be obtained by
        setting this to 1. Additional options for this parameter can be obtained
        by looking at parmetis.h. Default: 0.

      - options[2]: Random number seed for the routine

      - options[3]: Specifies whether the sub-domains and processors are coupled
        or un-coupled.  If the number of sub-domains desired (i.e., nparts) and
        the number of processors that are being used is not the same, then these
        must be un-coupled. However, if nparts equals the number of processors,
        these can either be coupled or de-coupled. If sub-domains and processors
        are coupled, then the initial partitioning will be obtained implicitly
        from the graph distribution. However, if sub-domains are un-coupled from
        processors, then the initial partitioning needs to be obtained from the
        initial values assigned to the part array.

    - itr: Parameter which describes the ratio of inter-processor communication
      time compared to data redistribution time.  Should be set between 0.000001
      and 1000000.0.  If set high, a repartitioning with a low edge-cut will be
      computed. If it is set low, a repartitioning that requires little data
      redistribution will be computed.  Good values for this parameter can be
      obtained by dividing inter-processor communication time by data
      redistribution time. Otherwise, a value of 1000.0 is recommended.
      Default: 1000.

The ParMETIS sources can be downloaded and compiled in ThirdParty-dev using the
link in the README file and the compilation commands in Allwmake.

Note the specific license under which ParMETIS is released:

Copyright & License Notice
--------------------------

The ParMETIS package is copyrighted by the Regents of the
University of Minnesota. It can be freely used for educational and
research purposes by non-profit institutions and US government
agencies only. Other organizations are allowed to use ParMETIS
only for evaluation purposes, and any further uses will require prior
approval. The software may not be sold or redistributed without prior
approval. One may make copies of the software for their use provided
that the copies, are not sold or distributed, are used under the same
terms and conditions.

As unestablished research software, this code is provided on an
``as is'' basis without warranty of any kind, either expressed or
implied. The downloading, or executing any part of this software
constitutes an implicit agreement to these terms. These terms and
conditions are subject to change at any time without prior notice.
2024-05-22 15:30:46 +01:00
41705e9eca Lagrangian: Added support for automatic run-time load-balancing
Optional CPU load caching can be switched-on for Lagrangian cloud tracking
and/or chemistry integration using the new cpuLoad switch in the cloudProperties
or chemistryProperties dictionary files respectively and used for
multi-constraint load-balancing by the fvMeshDistributorsLoadBalancer specified
in the dynamicMeshDict file

distributor
{
    type            loadBalancer;

    libs            ("libfvMeshDistributors.so");

    multiConstraint true;
    redistributionInterval  10;
}

which used the distributor specified in the decomposeParDict file, e.g.

numberOfSubdomains 12;

decomposer      simple;
distributor     zoltan;
libs            ("libzoltanDecomp.so");

simpleCoeffs
{
    n           (2 2 3);
}

zoltanCoeffs
{
    lb_method   rcb;
}

The incompressibleDenseParticleFluid/cyclone case has been updated to
demonstrate this new functionality and shows a speedup ~50% using the Zoltan RCB
multi-constraint distributor.  The multicomponentFluid/counterFlowFlame2D_GRI
case has also been updated to use the new cpuLoad switch.
2024-05-16 13:46:20 +01:00
41864093ca polyTopoChange::modifyCell: Replaced by direct specification of the cell zone 2024-03-12 14:08:10 +00:00
8331934c8c tutorials: removed blank lines left over from transferring the functions entry to the functions file 2024-01-21 10:50:32 +00:00
a1eb8898d6 tutorials: Moved the functions entry from controlDict into a functions file 2024-01-20 23:43:10 +00:00
6628a49daf tutorials: Updated for standardised thermo property names 2023-12-01 17:13:22 +00:00
e0bdf2405e fvModels: Remove 'Source' from names
The fact that these names create sources in their associated transport
equations is clear in context, so the name does not need to contain
'Source'.

Having 'Source' in the name is a historic convention that dates back to
when fvModels and fvConstraints were combined in a single fvOptions
interface. In this interface, disambiguation between sources and
constraints was necessary.

The full set of name changes is as follows:

                   accelerationSource -> acceleration
                  actuationDiskSource -> actuationDisk
     effectivenessHeatExchangerSource -> effectivenessHeatExchanger
               explicitPorositySource -> porosityForce
            radialActuationDiskSource -> radialActuationDisk
                      rotorDiskSource -> rotorDisk
             sixDoFAccelerationSource -> sixDoFAcceleration
         solidEquilibriumEnergySource -> solidThermalEquilibrium
          solidificationMeltingSource -> solidificationMelting
                 volumeFractionSource -> volumeBlockage
    interRegionExplicitPorositySource -> interRegionPorosityForce
       VoFSolidificationMeltingSource -> VoFSolidificationMelting

The old names are still available for backwards compatibility.
2023-10-13 09:53:32 +01:00
16ecc4fe08 fvConstraints: Remove 'Constraint' from constraint names
The fact that these names refer to constraints is clear in context, so
the name does not need to contain 'Constraint'.

Having 'Constraint' in the name is a historic convention that dates back
to when fvConstraints and fvModels were combined in a single fvOptions
interface. In this interface, disambiguation between sources and
constraints was necessary.

This change has been applied to the 'fixedValue' and 'fixedTemperature'
constraints, which were formerly named 'fixedValueConstraint' and
'fixedTemperatureConstraint', respectively.

The old names are still available for backwards compatibility.
2023-10-13 09:53:32 +01:00
171101d1e5 fvModels: Specify source property values in field files
When an fvModel source introduces fluid into a simulation it should also
create a corresponding source term for all properties transported into
the domain by that injection. The source is, effectively, an alternative
form of inlet boundary, on which all transported properties need an
inlet value specified.

These values are now specified in the property field files. The
following is an example of a 0/U file in which the velocity of fluid
introduced by a fvModel source called "injection1" is set to a fixed
value of (-1 0 0):

    dimensions      [0 1 -1 0 0 0 0];

    internalField   uniform (0 0 0);

    boundaryField
    {
        #includeEtc "caseDicts/setConstraintTypes"

        wall
        {
            type            noSlip;
        }

        atmosphere
        {
            type            pressureInletOutletVelocity;
            value           $internalField;
        }
    }

    // *** NEW ***
    sources
    {
        injection1
        {
            type            uniformFixedValue;
            uniformValue    (-1 0 0);
        }
    }

And the following entry in the 0/k file specifies the turbulent kinetic
energy introduced as a fraction of the mean flow kinetic energy:

    sources
    {
        injection1
        {
            type            turbulentIntensityKineticEnergy;
            intensity       0.05;
        }
    }

The specification is directly analogous to boundary conditions. The
conditions are run-time selectable and can be concisely implemented.
They can access each other and be inter-dependent (e.g., the above,
where turbulent kinetic energy depends on velocity). The syntax keeps
field data localised and makes the source model (e.g., massSource,
volumeSource, ...) specification independent from what other models and
fields are present in the simulation. The 'fieldValues' entry previously
required by source models is now no longer required.

If source values need specifying and no source condition has been
supplied in the relevant field file then an error will be generated.
This error is similar to that generated for missing boundary conditions.
This replaces the behaviour where sources such as these would introduce
a value of zero, either silently or with a warning. This is now
considered unacceptable. Zero might be a tolerable default for certain
fields (U, k), but is wholly inappropriate for others (T, epsilon, rho).

This change additionally makes it possible to inject fluid into a
multicomponent solver with a specified temperature. Previously, it was
not possible to do this as there was no means of evaluating the energy
of fluid with the injected composition.
2023-10-12 11:24:27 +01:00
87ff44aeb8 tutorials: Simplified dimensionless specification from [0 0 0 0 0 0 0] -> [] 2023-07-26 18:37:57 +01:00
568fb8e00e tutorials/multicomponentFluid/SandiaD_LTS: Updated to improve stability and convergence 2023-06-29 18:46:18 +01:00
5f0a643e71 tutorials/multicomponentFluid/counterFlowFlame2D: Clean 0/Qdot field 2023-06-29 11:27:29 +01:00
9fb9a8cc8c lagrangian: Merged parcel and parcelTurbulence libraries
Lagrangian's dependency set is simpler than it used to be. There is no
longer a need to maintain a separate library for models that depend on
the momentum transport modelling.
2023-06-27 15:44:54 +01:00
b51bb27fde tutorials/multicomponentFluid/lockExchange: Updated physicalProperties 2023-06-26 13:24:41 +01:00
2bb8cb9c9a tutorials/multicomponentFluid/membrane: Call foamRun rather than reactingFoam 2023-06-20 10:03:24 +01:00
025b96e217 tutorials/multicomponentFluid/verticalChannel: Corrected lagrangian mass flow rate 2023-06-16 15:22:57 +01:00
f1be983cda tutorials/multicomponentFluid/verticalChannel/system/particleTracksDict: Added setFormat entry 2023-06-16 15:05:45 +01:00
04dd989911 Time: Removed graphFormat
setFormat no longer defaults to the value of graphFormat optionally set in
controlDict and must be set in the functionObject dictionary.

boundaryFoam, financialFoam and pdfPlot still require a graphFormat entry in
controlDict but this is now read directly rather than by Time.
2023-06-16 14:51:30 +01:00
3eed5c0c99 lagrangian: InjectionModel: Time-varying parcel flow rate
The parcelsPerSecond control can now be specified as a time-varying
function. This provides additional control over the temporal
distribution of injected parcels, which may be advantageous if, for
example, the mass flow rate varies significantly. It also enables
variable flow rates of particulates in cases which have a fixed number
of particles per parcel.
2023-06-13 16:59:05 +01:00
da073b7d02 tutorials/multicomponentFluid/nc7h16/Allrun: Updated for the change in location of the chemFoam nc7h16 case 2023-05-27 17:12:20 +01:00
e744fdb5f1 Modular solvers: Reorganised directory structure of applications and tutorials
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
2023-05-25 18:14:41 +01:00