Commit Graph

43 Commits

Author SHA1 Message Date
a5ea0b41f1 fvModels: Improved interface for mass/volume sources
The interface for fvModels has been modified to improve its application
to "proxy" equations. That is, equations that are not straightforward
statements of conservation laws in OpenFOAM's usual convention.

A standard conservation law typically takes the following form:

    fvMatrix<scalar> psiEqn
    (
        fvm::ddt(alpha, rho, psi)
      + <fluxes>
     ==
        <sources>
    );

A proxy equation, on the other hand, may be a derivation or
rearrangement of a law like this, and may be linearised in terms of a
different variable.

The pressure equation is the most common example of a proxy equation. It
represents a statement of the conservation of volume or mass, but it is
a rearrangement of the original continuity equation, and it has been
linearised in terms of a different variable; the pressure. Another
example is that in the pre-predictor of a VoF solver the
phase-continuity equation is constructed, but it is linearised in terms
of volume fraction rather than density.

In these situations, fvModels sources are now applied by calling:

    fvModels().sourceProxy(<conserved-fields ...>, <equation-field>)

Where <conserved-fields ...> are (alpha, rho, psi), (rho, psi), just
(psi), or are omitted entirely (for volume continuity), and the
<equation-field> is the field associated with the proxy equation. This
produces a source term identical in value to the following call:

    fvModels().source(<conserved-fields ...>)

It is only the linearisation in terms of <equation-field> that differs
between these two calls.

This change permits much greater flexibility in the handling of mass and
volume sources than the previous name-based system did. All the relevant
fields are available, dimensions can be used in the logic to determine
what sources are being constructed, and sources relating to a given
conservation law all share the same function.

This commit adds the functionality for injection-type sources in the
compressibleVoF solver. A following commit will add a volume source
model for use in incompressible solvers.
2023-09-28 09:04:31 +01:00
da442e8eab multiphaseEuler: Replaced pPrime() with pPrimef()
to provide greater flexibility in the treatment of the face pPrime for particle
phase pressure models.
2023-09-22 16:16:49 +01:00
533421f91a multiphaseEuler: Removed redundant files 2023-09-21 13:09:01 +01:00
597121a4a7 multiphaseEuler: Library reorganisation
This change makes multiphaseEuler more consistent with other modules and
makes its sub-libraries less inter-dependent. Some left-over references
to multiphaseEulerFoam have also been removed.
2023-09-15 14:45:26 +01:00
9c3a404533 multiphaseEuler::cellPressureCorrector: Added p_rgh update before PISO loop
to ensure consistency between p_rgh, p and the current phase densities updated
after the phase energy solution.
2023-09-15 08:13:13 +01:00
c8a63f2da3 multiphaseEuler::phaseSystemSolve: Corrected handling of dilatation effects
in the presence of stationary phases
2023-09-14 20:52:41 +01:00
020463b64e multiphaseEuler::SolidThermalPhaseModel: New thermal phase model for solid phases
which provides the energy equation specific for stationary solid phases.
2023-09-14 16:33:52 +01:00
7b052fb6a1 multiphaseEuler::phaseInterface: Added stationary phase handling to magUr
This allows moving particle drag models to be used for stationary beds of particles.
2023-09-14 16:32:42 +01:00
d6caf68bce multiphaseEuler::correctCoNum: Corrected handling of stationary phases 2023-09-04 13:56:38 +01:00
3516b97a4d multiphaseEuler::setRDeltaT: Loop over the moving phases only to obtain maxPhi 2023-09-04 13:43:25 +01:00
17771b88d5 multiphaseEuler: Simplified using the movingPhase member reference 2023-09-03 16:27:02 +01:00
3c18db77ed multiphaseEuler::StationaryPhaseModel: Replaced functions returning 0 with notImplemented
requiring all parts of the moving phase solution algorithm to loop and operate
on the moving phases only making the code easier to understand and maintain.
2023-09-03 10:21:31 +01:00
ba772c03e6 multiphaseEuler::MomentumTransferPhaseSystem: Only cache the drag coefficients if needed
The virtual mass and face drag coefficients are no longer cached saving some
storage.
2023-09-01 22:55:50 +01:00
6558f63293 Merge branch 'master' of github.com-OpenFOAM:OpenFOAM/OpenFOAM-dev 2023-09-01 13:13:31 +01:00
18200e72a6 multiphaseEuler: Update the virtual-mass force implementation
The central coefficient part of the virtual-mass phase acceleration matrix is
now included in the phase velocity transport central coefficient + drag matrix
so that the all the phase contributions to each phase momentum equation are
handled implicitly and consistently without lagging contribution from the other
phases in either the pressure equation or phase momentum correctors.

This improves the conditioning of the pressure equation and convergence rate of
bubbly-flow cases.
2023-09-01 13:07:00 +01:00
eebd2d46d4 populationBalance: Fix typo 2023-08-31 13:42:53 +01:00
a83f23828b populationBalance: Corrected fraction field registration 2023-08-31 13:28:58 +01:00
a05df4abe0 populationBalance: Standardise default field handling
Population balance size-group fraction 'f<index>.<phase>' fields are now
read from an 'fDefault.<phase>' field if they are not provided
explicitly. This is the same process as is applied to species fractions
or fvDOM rays. The sum-of-fs field 'f.<phase>' is no longer required.

The value of a fraction field and its boundary conditions must now be
specified in the corresponding field file. Value entries are no longer
given in the size group dictionaries in the constant/phaseProperties
file, and an error message will be generated if a value entry is found.

The fraction fields are now numbered programatically, rather than being
named. So, the size-group dictionaries do not require a name any more.

All of the above is also true for any 'kappa<index>.<phase>' fields that
are constructed and solved for as part of a fractal shape model.

The following is an example of a specification of a population balance
with two phases in it:

    populationBalances (bubbles);

    air1
    {
        type            pureIsothermalPhaseModel;
        diameterModel   velocityGroup;
        velocityGroupCoeffs
        {
            populationBalance bubbles;
            shapeModel      spherical;
            sizeGroups
            (
                { dSph 1e-3; } // Size-group #0: Fraction field f0.air1
                { dSph 2e-3; } // ...
                { dSph 3e-3; }
                { dSph 4e-3; }
                { dSph 5e-3; }
            );
        }
        residualAlpha   1e-6;
    }

    air2
    {
        type            pureIsothermalPhaseModel;
        diameterModel   velocityGroup;
        velocityGroupCoeffs
        {
            populationBalance bubbles;
            shapeModel      spherical;
            sizeGroups
            (
                { dSph 6e-3; } // Size-group #5: Fraction field f5.air2
                { dSph 7e-3; } // ...
                { dSph 8e-3; }
                { dSph 9e-3; }
                { dSph 10e-3; }
                { dSph 11e-3; }
                { dSph 12e-3; }
            );
        }
        residualAlpha   1e-6;
    }

Previously a fraction field was constructed automatically using the
boundary condition types from the sum-of-fs field, and the value of both
the internal and boundary field was then overridden by the value setting
provided for the size-group. This procedure doesn't generalise to
boundary conditions other than basic types that store no additional
data, like zeroGradient and fixedValue. More complex boundary conditions
such as inletOutlet and uniformFixedValue are incompatible with this
approach.

This is arguably less convenient than the previous specification, where
the sizes and fractions appeared together in a table-like list in the
sizeGroups entry. In the event that a substantial proportion of the
size-groups have a non-zero initial fraction, writing out all the field
files manually is extremely tedious. To mitigate this somewhat, a
packaged function has been added to initialise the fields given a file
containing a size distribution (see the pipeBend tutorial for an example
of its usage). This function has the same limitations as the previous
code in that it requires all boundary conditions to be default
constructable.

Ultimately, the "correct" fix for the issue of how to set the boundary
conditions conveniently is to create customised inlet-outlet boundary
conditions that determine their field's position within the population
balance and evaluate a distribution to determine the appropriate inlet
value. This work is pending funding.
2023-08-31 12:05:12 +01:00
a0c391b8bd multiphaseEuler: Corrected handling of pRef 2023-08-30 14:16:09 +01:00
a91e7ea6d3 multiphaseEuler::MomentumTransferPhaseSystem::alphaDByAf: Only consider pPrime for moving phases 2023-08-30 13:32:20 +01:00
6054b1fea0 objectRegistry, regIOobject: Added support for automatic re-reading of dependent class
Now with the addition of the optional dependenciesModified() function classes
which depend on other classes which are re-read from file when modified are also
automatically updated via their read() function called by
objectRegistry::readModifiedObjects.

This significantly simplifies the update of the solutionControls and modular
solvers when either the controlDict or fvSolution dictionaries are modified at
run-time.
2023-08-28 20:28:39 +01:00
5fd30443f3 multiphaseEuler: New implicit drag algorithm replaces partial-elimination corrector
The momentum equation central coefficient and drag matrix is formulated,
inverted and used to eliminate the drag terms from each of the phase momentum
equations which are combined for formulate a drag-implicit pressure equation.
This eliminates the lagged drag terms from the previous formulation which
significantly improves convergence for small particle and Euler-VoF high-drag
cases.

It would also be possible to refactor the virtual-mass terms and include the
central coefficients of the phase acceleration terms in the drag matrix before
inversion to further improve the implicitness of the phase momentum-pressure
coupling for bubbly flows.  This work is pending funding.
2023-08-26 10:09:38 +01:00
e3b53f2727 multiphaseEuler: Fix indexing bug in partial elimination 2023-08-16 16:03:32 +01:00
2f579ca041 fluidSolvers: Stabilise rDeltaT calculation
When the flow is stationary (e.g., at the beginning of a run) the
rDeltaT calculation now requires a maxDeltaT setting in the PIMPLE
sub-section of the fvSolution dictionary. This prevents floating point
errors associated with rDeltaT approaching zero.
2023-07-27 12:16:05 +01:00
9cba18a073 Merge branch 'master' of github.com-OpenFOAM:OpenFOAM/OpenFOAM-dev 2023-07-27 10:58:46 +01:00
1e79d0245c MomentumTransferPhaseSystem::partialElimination: Removed the phase velocity mean adjustment
The phase velocity mean adjustment was introduced for consistency with phase
flux mean adjustment which is necessary to ensure the mean flux divergence is
preserved.  However for systems with very high drag it has proved preferable to
not adjust the velocity of the phases to conserve momentum rather than ensure
consistency with the fluxes.
2023-07-27 10:54:52 +01:00
4acddc6ab0 solidThermo: Add rhoThermo interface
The old fluid-specific rhoThermo has been split into a non-fluid
specific part which is still called rhoThermo, and a fluid-specific part
called rhoFluidThermo. The rhoThermo interface has been added to the
solidThermo model. This permits models and solvers that access the
density to operate on both solid and fluid thermophysical models.
2023-07-27 09:20:43 +01:00
3c542d664b thermophysicalModels: Primitive mixture classes
Mixture classes (e.g., pureMixtrure, coefficientMulticomponentMixture),
now have no fvMesh or volScalarField dependence. They operate on
primitive values only. All the fvMesh-dependent functionality has been
moved into the base thermodynamic classes. The 'composition()' access
function has been removed from multi-component thermo models. Functions
that were once provided by composition base classes such as
basicSpecieMixture and basicCombustionMixture are now implemented
directly in the relevant multi-component thermo base class.
2023-07-27 08:39:58 +01:00
d194e63820 controlDict::maxDeltaT: Changed to user-time for consistency with other time controls 2023-07-20 17:24:00 +01:00
2779442d2a functionObjects::fluidMaxDeltaT: New functionObject to set the maximum Courant number and time-step
at Function1s of time.

Underlying this new functionObject is a generalisation of the handling of the
maximum time-step in the modular solvers to allow complex user-specification of
the maximum time-step used in a simulation, not just the time-dependency
provided by fluidMaxDeltaT but functions of anything in the simulation by
creating a specialised functionObject in which the maxDeltaT function is
defined.

The chemical and combustion time-scale functionObjects adjustTimeStepToChemistry
and adjustTimeStepToCombustion have been updated and simplified using the above
mechanism.
2023-07-20 14:37:18 +01:00
6fce005097 multiphaseExternalTemperatureFvPatchScalarField: New multiphase version of externalTemperatureFvPatchScalarField
for the multiphaseEuler solver module, replacing the more specific
uniformFixedMultiphaseHeatFluxFvPatchScalarField as it provide equivalent
functionality if the heat-flux q is specified.

multiphaseExternalTemperatureFvPatchScalarField is derived from the refactored
and generalised externalTemperatureFvPatchScalarField, overriding the
getKappa member function to provide the multiphase equivalents of kappa and
other heat transfer properties.  All controls for
multiphaseExternalTemperatureFvPatchScalarField are the same as for
externalTemperatureFvPatchScalarField:

Class
    Foam::externalTemperatureFvPatchScalarField

Description
    This boundary condition applies a heat flux condition to temperature
    on an external wall. Heat flux can be specified in the following ways:

      - Fixed power: requires \c Q
      - Fixed heat flux: requires \c q
      - Fixed heat transfer coefficient: requires \c h and \c Ta

    where:
    \vartable
        Q  | Power Function1 of time [W]
        q  | Heat flux Function1 of time [W/m^2]
        h  | Heat transfer coefficient Function1 of time [W/m^2/K]
        Ta | Ambient temperature Function1 of time [K]
    \endvartable

    Only one of \c Q or \c q may be specified, if \c h and \c Ta are also
    specified the corresponding heat-flux is added.

    If the heat transfer coefficient \c h is specified an optional thin thermal
    layer resistances can also be specified through thicknessLayers and
    kappaLayers entries.

    The patch thermal conductivity \c kappa is obtained from the region
    thermophysicalTransportModel so that this boundary condition can be applied
    directly to either fluid or solid regions.

Usage
    \table
    Property     | Description                 | Required | Default value
    Q            | Power [W]                   | no       |
    q            | Heat flux [W/m^2]           | no       |
    h            | Heat transfer coefficient [W/m^2/K] | no |
    Ta           | Ambient temperature [K]     | if h is given  |
    thicknessLayers | Layer thicknesses [m]    | no |
    kappaLayers  | Layer thermal conductivities [W/m/K] | no |
    relaxation   | Relaxation for the wall temperature | no | 1
    emissivity   | Surface emissivity for radiative flux to ambient | no | 0
    qr           | Name of the radiative field | no | none
    qrRelaxation | Relaxation factor for radiative field | no | 1
    \endtable

    Example of the boundary condition specification:
    \verbatim
    <patchName>
    {
        type            externalTemperature;

        Ta              constant 300.0;
        h               uniform 10.0;
        thicknessLayers (0.1 0.2 0.3 0.4);
        kappaLayers     (1 2 3 4);

        value           $internalField;
    }
    \endverbatim

See also
    Foam::mixedFvPatchScalarField
    Foam::Function1
2023-07-15 21:50:14 +01:00
75106dcb62 uniformFixedMultiphaseHeatFluxFvPatchScalarField: Added fixesValue() returning false
so that the energy-> temperature conversion in *heThermo updates the wall
temperature.
2023-07-15 17:42:03 +01:00
2b3b820c90 Corrected duplicate word and it's typos 2023-07-11 11:02:47 +01:00
debd293832 Merge branch 'master' of github.com-OpenFOAM:OpenFOAM/OpenFOAM-dev 2023-06-16 21:36:54 +01:00
ef85d538e9 Changed stabilisation from rootVSmall to small for to avoid FPEs with extended precision 2023-06-16 21:36:05 +01:00
98ac903969 multiphaseEuler: Make energy predictor compatible with stationary phases 2023-06-16 16:23:56 +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
618d9d33b2 controlDict: the optional graphFormat entry is now used as the default for all setFormat entries
Foam::graph superseded by the more general Foam::setWriter reducing code
maintenance overhead, simplifying usage and further development.
2023-06-12 17:14:37 +01:00
0b8c17d8c1 functionObject,fvModel,fvConstraint: Added automatic library loading
If the libs entry is not provided and the name of the library containing the
functionObject, fvModel or fvConstraint corresponds to the type specified the
corresponding library is automatically loaded, e.g. to apply the
VoFTurbulenceDamping fvModel to an incompressibleVoF simulation the following
will load the libVoFTurbulenceDamping.so library automatically and instantiate
the fvModel:

turbulenceDamping
{
    type            VoFTurbulenceDamping;

    delta           1e-4;
}
2023-06-01 20:31:16 +01:00
fd6ef67d9f fvPatchFields: Removed unused null-constructors 2023-05-28 16:47:09 +01:00
8495fc9dc8 fvPatchField<Type>: Removed unused null-constructors 2023-05-28 08:40:08 +01:00
ca72b0a963 fvPatchFields: Removed all fvPatchFields requiring user specified data from the null-constructor table
This avoids potential hidden run-time errors caused by solvers running with
boundary conditions which are not fully specified.  Note that "null-constructor"
here means the constructor from patch and internal field only, no data is
provided.

Constraint and simple BCs such as 'calculated', 'zeroGradient' and others which
do not require user input to fully specify their operation remain on the
null-constructor table for the construction of fields with for example all
'calculated' or all 'zeroGradient' BCs.

A special version of the 'inletOutlet' fvPatchField named 'zeroInletOutlet' has
been added in which the inlet value is hard-coded to zero which allows this BC
to be included on the null-constructor table.  This is useful for the 'age'
functionObject to avoid the need to provide the 'age' volScalarField at time 0
unless special inlet or outlet BCs are required.  Also for isothermalFilm in
which the 'alpha' field is created automatically from the 'delta' field if it is
not present and can inherit 'zeroInletOutlet' from 'delta' if appropriate.  If a
specific 'inletValue' is require or other more complex BCs then the 'alpha'
field file must be provided to specify these BCs as before.

Following this improvement it will now be possible to remove the
null-constructors from all fvPatchFields not added to the null-constructor
table, which is most of them, thus reducing the amount of code and maintenance
overhead and making easier and more obvious to write new fvPatchField types.
2023-05-27 16:56:10 +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