Commit Graph

1790 Commits

Author SHA1 Message Date
adf6f25c0e compressibleMultiphaseInterFoam: Added missing fvModels.correct() 2022-02-15 18:34:16 +00:00
3b037cd6c3 multiphaseEulerFoam::phaseSystem: Added access to deltaN 2022-02-14 12:50:53 +00:00
5e8439aab1 setRDeltaT: Added support for optional minDeltaT
For some cases, in particular those with very small cells created by snapping in
corners for example, it may be beneficial to convergence rate to limit the
minimum LTS time-step, the new minDeltaT control provides this.
2022-02-10 15:57:46 +00:00
989cf27554 snappyHexMesh, createPatch: Keep all constraint patches even if zero size
This change ensures that special constraint type patches, like internal used for
load-balancing, are not deleted by snappyHexMesh or createPatch.
2022-02-10 14:47:07 +00:00
a2bfa0e911 multiphaseEulerFoam: noSintering: Corrected dimensions 2022-02-09 11:59:28 +00:00
c468a63830 compressibleInterFoam::VoFSurfaceFilm: Added maxDeltaT
to limit the time-step by comparing the film Courant number with the maximum
Courant number obtain from the optional maxCo entry in the system/<film
region>/fvSolution file.  If maxCo is not provided the film model does not limit
the time-step.

See tutorials/multiphase/compressibleInterFoam/laminar/cylinder as an example
demonstrating this functionality.
2022-02-09 11:45:42 +00:00
3ec5bf9257 setDeltaT: Simplified implementation 2022-02-09 11:44:20 +00:00
e478bb9b09 fvModels: Added maxDeltaT() function to provide a time-step limiter
fvModels.maxDeltaT() calls are now included in the setDeltaT.H files to
additionally limit the time-step if any fvModel require it.
2022-02-08 16:27:06 +00:00
e22870f508 compressibleMultiphaseInterFoam: Added contErr to avoid unboundedness in U and T 2022-02-08 16:25:44 +00:00
13b78294ff compressibleMultiphaseInterFoam: Added support for fvModels and fvConstraints 2022-02-08 16:25:10 +00:00
a7030ee97e CompactListList: Removed unnecessary templating and create unallocated base 2022-02-04 15:17:27 +00:00
66600b5497 chtMultiRegionFoam: Corrected multiple fluid region support for nEcorr
Resolves bug-report https://bugs.openfoam.org/view.php?id=3799
2022-02-04 15:05:53 +00:00
2fc40b7895 multiphaseEulerFoam: blending: Skip coefficient evaluation for constant case 2022-02-03 15:47:37 +00:00
39a8cb41a2 multiphaseEulerFoam: BlendedInterfacialModel: Fix for Clang 2022-02-01 15:09:55 +00:00
3c2fc7ca99 zeroDimensionalFvMesh: Centralised generation of zero-dimensional meshes 2022-01-28 17:25:22 +00:00
ba130ec083 multiphase: Rationalised alphaContactAngle handling
Alpha contact angle boundaries are now specified in the following way
for multiphase solvers (i.e., multiphaseInterFoam,
compressibleMultiphaseInterFoam, and multiphaseEulerFoam):

   boundaryField
   {
       wall
       {
           type            alphaContactAngle;
           contactAngleProperties
           {
               water
               {
                   // Constant contact angle
                   theta0 90;
               }
               oil
               {
                   // Dynamic contact angle
                   theta0 90;
                   uTheta 1;
                   thetaA 125;
                   thetaR 85;
               }
           }
           value           uniform 0;
       }
   }

All solvers now share the same implementation of the alphaContactAngle
boundary condition and the contact angle correction algorithm.

If alpha contact angle boundary conditions are used they must be
specified for all phases or an error will result. The consistency of the
input will also be checked. The angles given for water in the alpha.air
file must be 180 degrees minus the angles given for air in the
alpha.water file.
2022-01-28 17:25:22 +00:00
428c541680 multiphaseEulerFoam: Multiphase blending
Blending of sub-models has been extended so that it provides the
necessary functionality for the simulation of three or more phases.

Models now, by default, blend within the two-phase subset. So, the
functions which specify blending coefficients are evaluated using
`alpha1/(alpha1 + alpha2)` and `alpha2/(alpha1 + alpha2)`, rather than
just `alpha1` and `alpha2`. This ensures that the functions behave
consistently in multiphase configurations as the combined fraction of
both phases reduces.

Additional "displaced" categories of model are now available. These
allow the interface modelling to change as a third phase fraction
becomes significant and displaces the phases associated with the
interface in question. These can be specified using displaced phase
interfaces. If they are not supplied then the non-displaced models apply
instead.

Additional "general" categories are also now available. These span the
entire range of the subset's phase fraction space and apply if models
for the more specific configurations (i.e., displaced and segregated)
are omitted.

For example, to specify standard SchillerNaumann droplet/bubble drag
modelling outside of a solid bed, and the bed-specific AttouFerschneider
drag model within the bed, the following specification could be used:

    drag
    {
        air_dispersedIn_water
        {
            type            SchillerNaumann;
            residualRe      1e-3;
        }

        water_dispersedIn_air
        {
            $air_dispersedIn_water;
        }

        air_water_displacedBy_solid
        {
            type            AttouFerschneider;
            gas             air;
            liquid          water;
            solid           solid;
            E1              280;
            E2              4.8;
        }

        solid_dispersedIn_air
        {
            $air_water_displacedBy_solid;
        }

        solid_dispersedIn_water
        {
            $air_water_displacedBy_solid;
        }
    }

The "air_water_displacedBy_solid" model shown above is a
"general-displaced" model, in that its application does not depend on
dispersal of the air-water system; it only depends on the level of
displacement by the solid. Alternatively, a set of three
"dispersed-displaced" and "segregated-displaced" models could have been
provided with the following syntax:

        air_dispersedIn_water_displacedBy_solid
        {
            ...
        }

        air_segregatedWith_water_displacedBy_solid
        {
            ...
        }

        water_dispersedIn_air_displacedBy_solid
        {
            ...
        }

The blending methods themselves have changed slightly. There are now two
new methods; "segregated" for churning configurations in which no phase
is ever considered dispersed in another, and "continuous" where a
specified phase is always considered to be continuous and all other
phases are considered dispersed. These models replace the "none" model.

The linear and hyperbolic blending methods now support a "none" entry,
which can be set for parameters for phases that cannot become
continuous. For example, in an air-water-particles simulation the air
and water may become continuous, but the particles may not. A suitable
linear blending specification for this scenario might be as follows:

    blending
    {
        default
        {
            type            linear;
            minFullyContinuousAlpha.air 0.8;
            minPartlyContinuousAlpha.air 0.2;
            minFullyContinuousAlpha.water 0.8;
            minPartlyContinuousAlpha.water 0.2;
            minFullyContinuousAlpha.solid none;
            minPartlyContinuousAlpha.solid none;
        }
    }

The blending now provides far more feedback in terms of warnings and
errors when invalid or inadvisable specifications are made.

It is now also possible to visualise the various models' utilisation of
the phase fraction space. If the keyword "format" is placed in the
blending section of constant/phaseProperties then a plot (1 or 2 phases)
or surface (3 or more phases) file will be written out which shows the
phase fractions and the coefficients with which various models are
combined.
2022-01-28 09:24:28 +00:00
6bd200d0b5 multiphaseEulerFoam: New phaseInterface system to replace phasePair
A new class, phaseInterface, has been added to represent interfacial
configurations between pairs of phases. This class and its derivations
explicitly represent different configurations (e.g., dispersal,
segregation, displacement) by type and provide a run-time selection
mechanism so that these configurations can be uniquely named and
intuitively selected for sub-models to apply to.

For example, drag models can be selected for an air-water system with
full phase inversion with the following syntax in
constant/phaseProperties:

    drag
    {
        air_dispersedIn_water
        {
            type            IshiiZuber;
        }

        air_segregatedWith_water
        {
            type            segregated;
            m               0.5;
            n               8;
        }

        steam_dispersedIn_water
        {
            type            SchillerNaumann;
            residualRe      1e-3;
        }
    }

As well as the entries now being underscore separated, note also that
the sub model sections are now dictionaries ("{ ... }"), rather than
lists ("( ... );"). If a list is provided instead, then the input will
be considered to be in the old syntax, and will be read in a backwards
compatibility mode.

The new dictionary syntax permits substitution and therefore reuse of
settings, reducing the workload associated with setting up a large case
with many model combinations. In future it may be possible to introduce
wildcards to further reduce the verbosity of the input.

The new phase-interface classes and keywords and the phase-pairs and
keywords that they replace are listed below:

    Default/General:            phaseInterface "<phase>_<phase>"
                            replaces phasePair "(<phase> and <phase>)"

          Dispersed:   dispersedPhaseInterface "<phase>_dispersedIn_<phase>"
                     replaces orderedPhasePair "(<phase> in <phase>)"

         Segregated:  segregatedPhaseInterface "<phase>_segregatedWith_<phase>"
                            replaces phasePair "(<phase> and <phase>)"

              Sided:       sidedPhaseInterface "<phase>_<phase>_inThe_<phase>"
                     replaces orderedPhasePair "(<phase> in <phase>)"

          Displaced:   displacedPhaseInterface "<phase>_<phase>_displacedBy_<phase>"
                                        is new

Interface combinations are also possible. There can be, for example, an
interface which is both dispersed and sided. This class is the
dispersedSidedPhaseInterface and can be selected with the keyword
"<phase>_dispersedIn_<phase>_inThe_<phase>". This is needed, for
example, in two-resistance heat transfer modelling, where a different
model can be selected to represent heat transfer within the fluids on
either side of an interface.

A full list of all available phase interface relationships can be
generated by specifying an incorrect name, and viewing the output of the
error message that results.

The "displaced" interface is not currently used, but will shortly be
utilised to allowing the user to control how models between phases
change as the fraction of a third phase becomes significant and
displaces the phases associated with the interface in question.

Notes for developers:

There is no centralised storage of phase interface relationships in the
phase system any more; the table of phasePairs has been removed, and
there is no correcponding table of phaseInterfaces. Models now locally
store their own phaseInterface objects, or a derivation thereof, rather
than a reference to a centrally stored object. These phaseInterface
classes hold only references so there is no cost associated with their
duplication in multiple sub models.

If a model requires an interface of a specific type, it has to down-cast
the interface provided to it. There is a `phaseSystem::modelCast` method
for this purpose which also provides meaningful error messages in the
event that an inappropriate interface was specified and the cast fails.

Model generation is now hierarchical. Wrapper models (blended and sided)
are constructed with the same interface as non-wrapper models (drag,
virtual mass, etc...). The wrapper model constructors call the
constructors of their sub-models directly, rather than requiring model
pointers to be passed in.

Sub-model lookup has been significantly generalised and simplified.
There is now just one `phaseSystem::lookupInterfacialModel` method which
takes a phaseInterface as its argument. Looking up a model for a
specific configuration just requires providing the appropriate
phaseInterface. E.g., this call will return the virtual mass model for
gas bubbles in liquid:

    lookupSubModel<virtualMassModel>(dispersedPhaseInterface(gas, liquid))

Whilst this call will return the drag model for the segregated regime:

    lookupSubModel<dragModel>(segregatedPhaseInterface(phase1, phase2))

And this call will return the complete blended heat transfer model:

    lookupSubModel<blendedHeatTransferModel>(phaseInterface(phase1, phase2))
2022-01-28 09:24:15 +00:00
f4b497bd81 driftFluxFoam::mixtureViscosityModels: Added the basic Quemada viscosity model for for colloidal dispersions
currently without strain-rate dependency.

Class
    Foam::mixtureViscosityModels::Quemada

Description
     Quemada viscosity model for for colloidal dispersions.

     References:
     \verbatim
         Quemada, D. (1998).
         Rheological modelling of complex fluids. I.
         The concept of effective volume fraction revisited.
         The European Physical Journal-Applied Physics, 1(1), 119-127.
    \endverbatim

Usage
    Example usage:
    \verbatim
    viscosityModel  Quemada;

    alphaMax    0.6; // Maximum dispersed phase-fraction (packing fraction)
    q           2;   // Exponent, defaults to 2

    rho         1996;
    \endverbatim
2022-01-26 15:25:30 +00:00
8cb90dab4f functionObjectList: Improved error message if a functionObject configuration file is not foundation
e.g. if streamlinesLines is specified rather than the correct streamlinesLine in
the controlDict::functions list:

functions
{
    #includeFunc streamlinesLines
    (
        funcName=streamlines,
        start=(-0.0205 0.001 0.00001),
        end=(-0.0205 0.0251 0.00001),
        nPoints=10,
        fields=(p k U)
    )
}

the following error message is generated providing a list of all the
functionObject configuration files available and the run stops rather than
continuing regardless of the error:

--> FOAM FATAL IO ERROR:
Cannot find functionObject configuration file streamlinesLines

Available configured functionObjects:
88
(
CourantNo
Lambda2
MachNo
PecletNo
Q
Qdot
XiReactionRate
add
age
boundaryProbes
cellMax
cellMaxMag
cellMin
cellMinMag
components
cutPlaneSurface
ddt
div
divide
dsmcFields
enstrophy
faceZoneAverage
faceZoneFlowRate
fieldAverage
flowType
forceCoeffsCompressible
forceCoeffsIncompressible
forcesCompressible
forcesIncompressible
grad
graphCell
graphCellFace
graphFace
graphLayerAverage
graphUniform
interfaceHeight
internalProbes
isoSurface
log
mag
magSqr
moments
multiply
particles
patchAverage
patchDifference
patchFlowRate
patchIntegrate
patchSurface
phaseForces
phaseMap
phaseScalarTransport
probes
randomise
residuals
scalarTransport
scale
shearStress
sizeDistribution
staticPressureIncompressible
stopAtClockTime
stopAtFile
streamFunction
streamlinesLine
streamlinesPatch
streamlinesPoints
streamlinesSphere
subtract
surfaceInterpolate
time
timeStep
totalEnthalpy
totalPressureCompressible
totalPressureIncompressible
triSurfaceDifference
triSurfaceVolumetricFlowRate
turbulenceFields
turbulenceIntensity
uniform
vorticity
wallHeatFlux
wallHeatTransferCoeff
wallShearStress
writeCellCentres
writeCellVolumes
writeObjects
writeVTK
yPlus
)

file: /home/dm2/henry/OpenFOAM/OpenFOAM-dev/tutorials/incompressible/simpleFoam/pitzDaily/system/controlDict/functions

    From function static bool Foam::functionObjectList::readFunctionObject(const Foam::string&, Foam::dictionary&, const Foam::Pair<Foam::string>&, const Foam::word&)
    in file db/functionObjects/functionObjectList/functionObjectList.C at line 250.

FOAM exiting
2022-01-26 12:02:07 +00:00
a033b7276f functionObjects: writeVTK: Fixes
The lookup been fixed to prevent failures when a field is looked up with
the wrong type, and it now also provides warnings when a field cannot be
found for any type.
2022-01-25 10:26:06 +00:00
66f325fc41 multiphaseEulerFoam: Add "none" diameterModel for phases that are always continuous
This model will generate an error if the diameter is requested. This
will happen if another sub model is included that depends on the
diameter of the continuous phase. It therefore provides a check that the
sub-modelling combination is valid.

Patch contributed by Institute of Fluid Dynamics,
Helmholtz-Zentrum Dresden - Rossendorf (HZDR)
2022-01-19 15:21:06 +00:00
3cc9475b45 multiphaseEulerFoam: Added reporting of selected binary breakup model
Patch contributed by Institute of Fluid Dynamics,
Helmholtz-Zentrum Dresden - Rossendorf (HZDR)
2022-01-19 15:15:05 +00:00
bf3ec0eb87 multiphaseEulerFoam: populationBalance: Removed unused header includes
Patch contributed by Institute of Fluid Dynamics,
Helmholtz-Zentrum Dresden - Rossendorf (HZDR)
2022-01-19 15:13:31 +00:00
ded017b762 mapFields: Corrected handling of userTime
Resolves bug-report https://bugs.openfoam.org/view.php?id=3786
2022-01-18 10:52:06 +00:00
40286ba59e setAtmBoundaryLayer: New initialisation utility
This utility initialises the U, k and epsilon fields (if available) to
the output of the atmBoundaryLayer model. This is the same model as used
in the atmBoundaryLayerInlet.* boundary conditions and in the
waveAtmBoundaryLayer wave model.

The settings for the initialisation are read from a
system/setAtmBoundaryLayerDict file and are identical to the settings
required by the other use cases. An example of the settings required
within a system/setAtmBoundaryLayerDict file is shown below:

    zDir            (0 0 1);        // Vertical direction
    flowDir         (1 0 0);        // Direction of far-field flow
    Zref            20;             // Reference height
    Uref            10;             // Speed at reference height
    z0              uniform 0.1;    // Roughness height
    zGround         uniform 0;      // Ground height
2022-01-14 17:13:09 +00:00
62ad471222 multiphaseEulerFoam: Made segregated drag model numerically symmetric 2022-01-13 10:12:20 +00:00
30c877a7ab multiphaseEulerFoam: Use phaseSystem::propertiesName 2022-01-13 10:12:20 +00:00
3f1bb7ee13 multiphaseEulerFoam: Minor fixes to population balance function objects
Patch contributed by Institute of Fluid Dynamics,
Helmholtz-Zentrum Dresden - Rossendorf (HZDR)
2022-01-11 14:07:01 +00:00
32b656f8a7 multiphaseEulerFoam, turbulentDispersionModel: Corrected face-force for multiphase case
This is a completion of commit 64da7a2c. The fix has now also been
applied to the face-momentum equation.
2022-01-11 13:55:46 +00:00
cc96abda03 basicThermo: Cache thermal conductivity kappa rather than thermal diffusivity alpha
Now that Cp and Cv are cached it is more convenient and consistent and slightly
more efficient to cache thermal conductivity kappa rather than thermal
diffusivity alpha which is not a fundamental property, the appropriate form
depending on the energy solved for.  kappa is converted into the appropriate
thermal diffusivity for the energy form solved for by dividing by the
corresponding cached heat capacity when required, which is efficient.
2022-01-10 20:19:00 +00:00
794255284f multiphaseEulerFoam: revised sizeDistribution functionObject
Following the addition of the new moments functionObject, all related
functionality was removed from sizeDistribution.

In its revised version, sizeDistribution allows for different kinds of
weighted region averaging in case of field-dependent representative
particle properties.

A packaged function has also been added to allow for command line solver
post-processing.

For example, the following function object specification returns the
volume-based number density function:

    numberDensity
    {
        type                sizeDistribution;
        libs                ("libmultiphaseEulerFoamFunctionObjects.so");
        writeControl        writeTime;
        populationBalance   bubbles;
        functionType        numberDensity;
        coordinateType      volume;
        setFormat           raw;
    }

The same can be achieved using a packaged function:

    #includeFunc sizeDistribution
    (
        populationBalance=bubbles,
        functionType=numberDensity,
        coordinateType=volume,
        funcName=numberDensity
    )

Or on the command line:

    multiphaseEulerFoam -postProcess -func "
    sizeDistribution
    (
        populationBalance=bubbles,
        functionType=numberDensity,
        coordinateType=volume,
        funcName=numberDensity
    )"

Patch contributed by Institute of Fluid Dynamics,
Helmholtz-Zentrum Dresden - Rossendorf (HZDR)
2022-01-07 09:48:30 +00:00
36c565b9bf multiphaseEulerFoam: new functionObject "moments"
This function calculates integral (integer moments) or mean properties
(mean, variance, standard deviation) of a size distribution computed with
multiphaseEulerFoam. It has to be run with multiphaseEulerFoam, either
at run-time or with -postProcess. It will not work with the postProcess
utility.

The following function object specification for example returns the first
moment of the volume-based number density function which is equivalent to
the phase fraction of the particulate phase:

    moments
    {
        type                moments;
        libs                ("libmultiphaseEulerFoamFunctionObjects.so");
        executeControl      timeStep;
        writeControl        writeTime;
        populationBalance   bubbles;
        momentType          integerMoment;
        coordinateType      volume;
        order               1;
    }

The same can be achieved using a packaged function:

    #includeFunc moments
    (
        populationBalance=bubbles,
        momentType=integerMoment,
        coordinateType=volume,
        order=1,
        funcName=moments
    )

Or on the command line:

    multiphaseEulerFoam -postProcess -func "
        moments
        (
            populationBalance=bubbles,
            momentType=integerMoment,
            coordinateType=volume,
            order=1,
            funcName=moments
        )"

Patch contributed by Institute of Fluid Dynamics,
Helmholtz-Zentrum Dresden - Rossendorf (HZDR)
2022-01-07 09:48:30 +00:00
1b116fdddd Allwmake: use wmake -a to replace (cd ... && ./Allwmake... 2022-01-03 16:42:40 +00:00
dbf600af43 lagrangian: Added interface for mesh redistribution 2021-12-26 12:03:45 +00:00
9691eb13a6 compressibleInterFoam::VoFClouds: Added prototype call to redistribute the clouds 2021-12-24 17:17:01 +00:00
5ed8dbb463 fvModels: Added support for mesh redistribution and load-balancing 2021-12-24 15:02:30 +00:00
526b3840c7 renumberMethods::zoltanRenumber: set default ORDER_METHOD to LOCAL_HSFC
also adding optional "libs" entry to renumberMeshDict so that the
libzoltanRenumber.so can be loaded at run-time rather than having to recompile
and relink the renumberMesh utility to support it.
2021-12-20 22:48:37 +00:00
ad20aecf0e surfaceFilmModel: film model selection now handled by fvModel
There is no longer any need for the surfaceFilmModel abstract base class and
"New" selection method as surface films are now handled within the fvModel
framework.  This makes the surfaceFilmModel entry in the surfaceFilmProperties
dictionary redundant.

The surfaceFilm and VoFSurfaceFilm fvModels now instantiate a thermoSingleLayer
providing direct access to all the film functions, simplifying the
implementation better ensuring consistency between the film and primary region
equations.
2021-12-16 20:51:08 +00:00
f97f6326f0 Decomposition/redistribution: Separated choice of mesh decomposition and redistribution methods
When snappyHexMesh is run in parallel it re-balances the mesh during refinement
and layer addition by redistribution which requires a decomposition method
that operates in parallel, e.g. hierachical or ptscotch.  decomposePar uses a
decomposition method which operates in serial e.g. hierachical but NOT
ptscotch.  In order to run decomposePar followed by snappyHexMesh in parallel it
has been necessary to change the method specified in decomposeParDict but now
this is avoided by separately specifying the decomposition and distribution
methods, e.g. in the incompressible/simpleFoam/motorBike case:

numberOfSubdomains  6;

decomposer      hierarchical;
distributor     ptscotch;

hierarchicalCoeffs
{
    n               (3 2 1);
    order           xyz;
}

The distributor entry is also used for run-time mesh redistribution, e.g. in the
multiphase/interFoam/RAS/floatingObject case re-distribution for load-balancing
is enabled in constant/dynamicMeshDict:

distributor
{
    type            distributor;

    libs            ("libfvMeshDistributors.so");

    redistributionInterval  10;
}

which uses the distributor specified in system/decomposeParDict:

distributor     hierarchical;

This rationalisation provides the structure for development of mesh
redistribution and load-balancing.
2021-12-15 22:12:00 +00:00
dc0786239f Merge branch 'master' of github.com-OpenFOAM:OpenFOAM/OpenFOAM-dev 2021-12-15 11:45:36 +00:00
d90f421841 zoltanRenumber: Updated, corrected and tested 2021-12-15 11:45:11 +00:00
3761c48e1c multiphaseEulerFoam: Make aspect ratio models sub-models of force models
These models are quite configuration specific. It makes sense to make
them sub-models of the force (drag or lift) models that use them, rather
than making them fundamental properties of the phase system.
2021-12-14 11:26:16 +00:00
491f355d97 multiphaseEulerFoam, phasePair: Made aspect ratio method consistent 2021-12-09 21:08:02 +00:00
1548508149 multiphaseEulerFoam, BlendedInterfacialModel: Removed unused constructor 2021-12-09 21:08:02 +00:00
72687d3e46 multiphaseEulerFoam, dragModel: Removed unused constructor 2021-12-09 09:14:36 +00:00
053eed714d functionObjects: layerAverage: Replacment for postChannel
This function generates plots of fields averaged over the layers in the
mesh. It is a generalised replacement for the postChannel utility, which
has been removed. An example of this function's usage is as follows:

    layerAverage1
    {
        type            layerAverage;
        libs            ("libfieldFunctionObjects.so");

        writeControl    writeTime;

        setFormat       raw;

        // Patches and/or zones from which layers extrude
        patches         (bottom);
        zones           (quarterPlane threeQuartersPlane);

        // Spatial component against which to plot
        component       y;

        // Is the geometry symmetric around the centre layer?
        symmetric       true;

        // Fields to average and plot
        fields          (pMean pPrime2Mean UMean UPrime2Mean k);
    }
2021-12-08 12:48:54 +00:00
5d93da3aed snappyHexMesh: Added castellatedMeshControls:extendedRefinementSpan option
The code relating to extending refinement to the span of the facet/triangles
intersected by the refinement distance referred to in report

https://bugs.openfoam.org/view.php?id=3361

and temporarily removed may now be selected by the optional
castellatedMeshControls:extendedRefinementSpan entry in snappyHexMeshDict.  It
in not clear if this control is generally beneficial and very few users have
reported a preference and too few example cases have been provided to make a
balanced judgement so it has been decided to reinstate the previous default
behaviour and default extendedRefinementSpan to true.
2021-12-07 12:17:52 +00:00
25a6d068f0 sampledSets, streamlines: Various improvements
Sampled sets and streamlines now write all their fields to the same
file. This prevents excessive duplication of the geometry and makes
post-processing tasks more convenient.

"axis" entries are now optional in sampled sets and streamlines. When
omitted, a default entry will be used, which is chosen appropriately for
the coordinate set and the write format. Some combinations are not
supported. For example, a scalar ("x", "y", "z" or "distance") axis
cannot be used to write in the vtk format, as vtk requires 3D locations
with which to associate data. Similarly, a point ("xyz") axis cannot be
used with the gnuplot format, as gnuplot needs a single scalar to
associate with the x-axis.

Streamlines can now write out fields of any type, not just scalars and
vectors, and there is no longer a strict requirement for velocity to be
one of the fields.

Streamlines now output to postProcessing/<functionName>/time/<file> in
the same way as other functions. The additional "sets" subdirectory has
been removed.

The raw set writer now aligns columns correctly.

The handling of segments in coordSet and sampledSet has been
fixed/completed. Segments mean that a coordinate set can represent a
number of contiguous lines, disconnected points, or some combination
thereof. This works in parallel; segments remain contiguous across
processor boundaries. Set writers now only need one write method, as the
previous "writeTracks" functionality is now handled by streamlines
providing the writer with the appropriate segment structure.

Coordinate sets and set writers now have a convenient programmatic
interface. To write a graph of A and B against some coordinate X, in
gnuplot format, we can call the following:

    setWriter::New("gnuplot")->write
    (
        directoryName,
        graphName,
        coordSet(true, "X", X), // <-- "true" indicates a contiguous
        "A",                    //     line, "false" would mean
        A,                      //     disconnected points
        "B",
        B
    );

This write function is variadic. It supports any number of
field-name-field pairs, and they can be of any primitive type.

Support for Jplot and Xmgrace formats has been removed. Raw, CSV,
Gnuplot, VTK and Ensight formats are all still available.

The old "graph" functionality has been removed from the code, with the
exception of the randomProcesses library and associated applications
(noise, DNSFoam and boxTurb). The intention is that these should also
eventually be converted to use the setWriters. For now, so that it is
clear that the "graph" functionality is not to be used elsewhere, it has
been moved into a subdirectory of the randomProcesses library.
2021-12-07 11:18:27 +00:00
50fb2477bd compressibleInterFoam::pEqn: Limit pressure after calculating flux and dilatation rate
to avoid spurious phase-change from an inconsistency between the flux and the
dilatation rate that the pressure limiting might generate.
2021-12-06 23:12:19 +00:00