Commit Graph

434 Commits

Author SHA1 Message Date
2867696459 dragModels: Tenneti: Corrected Doxygen formatting 2017-10-10 15:26:07 +01:00
8315fe0196 MultiComponentPhaseModel: Included laminar diffusion in YiEqns
Resolves bug report https://bugs.openfoam.org/view.php?id=2591
2017-10-03 08:58:24 +01:00
adb66dd625 reactingTwoPhaseEulerFoam: Added continuity fvOption term to U equations
Patch contributed by Juho Peltola, VTT
Resolves bug-report https://bugs.openfoam.org/view.php?id=2699
2017-09-15 11:43:15 +01:00
018adc16c9 Corrected file conditional compilation macro names to be consistency with the file names
Scripts contributed by Bruno Santos
Resolves request https://bugs.openfoam.org/view.php?id=2692#c8735
2017-09-12 13:39:48 +01:00
0ad0d34b42 limitTemperature: added support for multiphase solvers
Based on patch contributed by Juho Peltola, VTT

Resolves feature request https://bugs.openfoam.org/view.php?id=2572
2017-09-04 16:52:03 +01:00
92ef068675 compressibleMultiphaseInterFoam: Corrected update of dgdt for multiple phases
Resolves bug-report https://bugs.openfoam.org/view.php?id=2677
2017-08-29 14:48:32 +01:00
82675f0976 Merged reactingParcelFilmFoam into reactingParcelFoam
The combined solver includes the most advanced and general functionality from
each solver including:

    Continuous phase
    Lagrangian multiphase parcels
    Optional film
    Continuous and Lagrangian phase reactions
    Radiation
    Strong buoyancy force support by solving for p_rgh

The reactingParcelFoam and reactingParcelFilmFoam tutorials have been combined
and updated.
2017-08-29 09:33:45 +01:00
c57fe2b5fd MRF: Added support for mesh refinement/unrefinement and other topology changes 2017-08-18 22:22:47 +01:00
53a524a280 Simplified scalar(0.0) -> scalar(0) and scalar(1.0) -> scalar(1) 2017-07-21 17:37:37 +01:00
14473273e9 compressibleInterFilmFoam::VoFSolidificationMeltingSource: New VoF solidification fvOption 2017-07-20 18:15:27 +01:00
593df2e92a Removed unintended integer divisions 2017-07-13 09:23:11 +01:00
2b05ad16b2 dragModels::Ergun: Corrected leading coefficient
Resolves bug report https://bugs.openfoam.org/view.php?id=2612
2017-07-13 08:47:47 +01:00
7c301dbff4 Parallel IO: New collated file format
When an OpenFOAM simulation runs in parallel, the data for decomposed fields and
mesh(es) has historically been stored in multiple files within separate
directories for each processor.  Processor directories are named 'processorN',
where N is the processor number.

This commit introduces an alternative "collated" file format where the data for
each decomposed field (and mesh) is collated into a single file, which is
written and read on the master processor.  The files are stored in a single
directory named 'processors'.

The new format produces significantly fewer files - one per field, instead of N
per field.  For large parallel cases, this avoids the restriction on the number
of open files imposed by the operating system limits.

The file writing can be threaded allowing the simulation to continue running
while the data is being written to file.  NFS (Network File System) is not
needed when using the the collated format and additionally, there is an option
to run without NFS with the original uncollated approach, known as
"masterUncollated".

The controls for the file handling are in the OptimisationSwitches of
etc/controlDict:

OptimisationSwitches
{
    ...

    //- Parallel IO file handler
    //  uncollated (default), collated or masterUncollated
    fileHandler uncollated;

    //- collated: thread buffer size for queued file writes.
    //  If set to 0 or not sufficient for the file size threading is not used.
    //  Default: 2e9
    maxThreadFileBufferSize 2e9;

    //- masterUncollated: non-blocking buffer size.
    //  If the file exceeds this buffer size scheduled transfer is used.
    //  Default: 2e9
    maxMasterFileBufferSize 2e9;
}

When using the collated file handling, memory is allocated for the data in the
thread.  maxThreadFileBufferSize sets the maximum size of memory in bytes that
is allocated.  If the data exceeds this size, the write does not use threading.

When using the masterUncollated file handling, non-blocking MPI communication
requires a sufficiently large memory buffer on the master node.
maxMasterFileBufferSize sets the maximum size in bytes of the buffer.  If the
data exceeds this size, the system uses scheduled communication.

The installation defaults for the fileHandler choice, maxThreadFileBufferSize
and maxMasterFileBufferSize (set in etc/controlDict) can be over-ridden within
the case controlDict file, like other parameters.  Additionally the fileHandler
can be set by:
- the "-fileHandler" command line argument;
- a FOAM_FILEHANDLER environment variable.

A foamFormatConvert utility allows users to convert files between the collated
and uncollated formats, e.g.
    mpirun -np 2 foamFormatConvert -parallel -fileHandler uncollated

An example case demonstrating the file handling methods is provided in:
$FOAM_TUTORIALS/IO/fileHandling

The work was undertaken by Mattijs Janssens, in collaboration with Henry Weller.
2017-07-07 11:39:56 +01:00
aa1712de8f VoFPatchTransfer: Corrected for clang 2017-07-07 11:03:12 +01:00
3193fdb667 compressibleInterFilmFoam: Added to Allwmake 2017-07-07 09:27:35 +01:00
f628af00a8 compressibleInterFilmFoam::VoFPatchTransfer: Remove requirement for film to be present before VoF->film transfers occur 2017-07-05 16:49:44 +01:00
2d866e281b compressibleInterFilmFoam::VoFPatchTransfer: corrected parallel handling of all patch option 2017-06-28 15:03:40 +01:00
d74f354f0c compressibleInterFilmFoam: Experimental VoF solver supporting VoF<->film transfer 2017-06-27 15:55:43 +01:00
21aeea88a4 saturationModels::function1: New Function1 Tsat model
based on code contributed by Juho Peltola, VTT.

Resolves contribution request https://bugs.openfoam.org/view.php?id=2573
2017-06-26 17:36:10 +01:00
47f64c6ed7 reactingEulerFoam: Bug fix to reactionsource terms
Fixed reaction source terms in the energy and species fraction equations
by multiplying by the phase fraction.

Resolves bug report https://bugs.openfoam.org/view.php?id=2591
2017-06-26 17:05:35 +01:00
5caadae42b reactingMultiphaseEulerFoam: Limited phase-fractions
for consistency with reactingTwoPhaseEulerFoam and to ensure correct operation
of models requiring formal boundedness of phase-fractions.

Resolves bug-report https://bugs.openfoam.org/view.php?id=2589
2017-06-26 16:24:57 +01:00
e8daaa5c76 compressibleInterFoam: Improved mass conservation
using the continuity error correction formulation developed for
twoPhaseEulerFoam and reactingEulerFoam.
2017-06-22 14:42:36 +01:00
7bdbab7f4e Rationalize the "pos" function
"pos" now returns 1 if the argument is greater than 0, otherwise it returns 0.
This is consistent with the common mathematical definition of the "pos" function:

https://en.wikipedia.org/wiki/Sign_(mathematics)

However the previous implementation in which 1 was also returned for a 0
argument is useful in many situations so the "pos0" has been added which returns
1 if the argument is greater or equal to 0.  Additionally the "neg0" has been
added which returns 1 if if the argument is less than or equal to 0.
2017-06-22 14:32:18 +01:00
77ade5a706 reactingEulerFoam::IsothermalPhaseModel: Added support for isothermal compressible flow
Based on patch contributed by Ronald Oertel, HZDR
Resolves bug-report https://bugs.openfoam.org/view.php?id=2583
2017-06-15 16:43:04 +01:00
79ff91350e rhoPimpleFoam: Improved support for compressible liquids
See tutorials/compressible/rhoPimpleFoam/RAS/squareBendLiq for exapmle

pimpleControl: Added SIMPLErho option for running in SIMPLE mode

with large time-step/Courant number and relaxation.  With this option the
density is updated from thermodynamics rather than continuity after the pressure
equation which is better behaved if pressure is relaxed and/or solved to a
loose relative tolerance.  The need for this option is demonstrated in the
tutorials/compressible/rhoPimpleFoam/RAS/angledDuct tutorial which is unstable
without the option.
2017-05-17 17:05:43 +01:00
9fbe68fca6 Replacing const_cast lookupObject to lookupObjectRef 2017-05-11 14:42:59 +01:00
80c101b14f Euler-Euler: turbulentDispersionModels: Burns: Minor re-formulation to
improve stability.

Resolves bug report <https://bugs.openfoam.org/view.php?id=2544>
2017-05-09 08:55:29 +01:00
7863708489 reactingEulerFoam: Corrected definition of Reynolds number in Beetstra and Tenneti drag laws
Patch contributed by Alberto Passalacqua, Iowa State University
2017-05-03 19:18:30 +01:00
1328b5be0f surfaceTensionModels: Resolved warning from Clang concerning virtual function overload 2017-05-03 19:17:43 +01:00
8514ff55d0 VoF solvers: New interfaceCompressionFvPatchScalarField BC and additional shear compression
Provides the additional compression necessary to ensure interface integrity
adjacent to a boundary at a low angle of incidence to the interface.  This is
particularly important when simulating planing hulls.
2017-04-30 19:38:47 +01:00
9801c25788 The "<type>Coeffs" sub-dictionary is now optional for most model parameters
except turbulence and lagrangian which will also be updated shortly.

For example in the nonNewtonianIcoFoam offsetCylinder tutorial the viscosity
model coefficients may be specified in the corresponding "<type>Coeffs"
sub-dictionary:

transportModel  CrossPowerLaw;

CrossPowerLawCoeffs
{
    nu0         [0 2 -1 0 0 0 0]  0.01;
    nuInf       [0 2 -1 0 0 0 0]  10;
    m           [0 0 1 0 0 0 0]   0.4;
    n           [0 0 0 0 0 0 0]   3;
}

BirdCarreauCoeffs
{
    nu0         [0 2 -1 0 0 0 0]  1e-06;
    nuInf       [0 2 -1 0 0 0 0]  1e-06;
    k           [0 0 1 0 0 0 0]   0;
    n           [0 0 0 0 0 0 0]   1;
}

which allows a quick change between models, or using the simpler

transportModel  CrossPowerLaw;

nu0         [0 2 -1 0 0 0 0]  0.01;
nuInf       [0 2 -1 0 0 0 0]  10;
m           [0 0 1 0 0 0 0]   0.4;
n           [0 0 0 0 0 0 0]   3;

if quick switching between models is not required.

To support this more convenient parameter specification the inconsistent
specification of seedSampleSet in the streamLine and wallBoundedStreamLine
functionObjects had to be corrected from

    // Seeding method.
    seedSampleSet   uniform;  //cloud; //triSurfaceMeshPointSet;

    uniformCoeffs
    {
        type        uniform;
        axis        x;  //distance;

        // Note: tracks slightly offset so as not to be on a face
        start       (-1.001 -0.05 0.0011);
        end         (-1.001 -0.05 1.0011);
        nPoints     20;
    }

to the simpler

    // Seeding method.
    seedSampleSet
    {
        type        uniform;
        axis        x;  //distance;

        // Note: tracks slightly offset so as not to be on a face
        start       (-1.001 -0.05 0.0011);
        end         (-1.001 -0.05 1.0011);
        nPoints     20;
    }

which also support the "<type>Coeffs" form

    // Seeding method.
    seedSampleSet
    {
        type        uniform;

        uniformCoeffs
        {
            axis        x;  //distance;

            // Note: tracks slightly offset so as not to be on a face
            start       (-1.001 -0.05 0.0011);
            end         (-1.001 -0.05 1.0011);
            nPoints     20;
        }
    }
2017-04-20 09:14:48 +01:00
d96a221b31 Admin: fixed file permissions from wall boiling model refinements 2017-04-16 18:27:19 +01:00
95ab9a5f67 reactingtwoPhaseEulerFoam: Wall boiling model refinements
Patch contributed by Juho Peltola, VTT.

Resolves patch request https://bugs.openfoam.org/view.php?id=2521
2017-04-12 14:31:35 +01:00
0fa88b8de4 tutorials/multiphase/reactingTwoPhaseEulerFoam/laminar/steamInjection: Improved stability
Main changes in the tutorial:
  - General cleanup of the phaseProperties of unnecessary entries
  - sensibleEnthalpy is used for both phases
  - setTimeStep functionObject is used to set a sharp reduction in time step near the start of the injection
  - Monitoring of pressure minimum and maximum

Patch contributed by Juho Peltola, VTT.
2017-04-11 20:48:32 +01:00
76579f5814 surfaceTensionModels::liquidProperties: New temperature-dependent surface tension model
Description
    Temperature-dependent surface tension model in which the surface tension
    function provided by the phase Foam::liquidProperties class is used.

Usage
    \table
        Property     | Description               | Required    | Default value
        phase        | Phase name                | yes         |
    \endtable

    Example of the surface tension specification:
    \verbatim
        sigma
        {
            type    liquidProperties;
            phase   water;
        }
    \endverbatim

for use with e.g. compressibleInterFoam, see
tutorials/multiphase/compressibleInterFoam/laminar/depthCharge2D
2017-04-05 14:36:11 +01:00
79a050573b tutorials/multiphase: Removed unnecessary specification of name and dimensions for transport properties 2017-03-31 17:11:30 +01:00
cf0b6126d0 surfaceTensionModels: New class hierarchy for run-time selectable surface tension models
These models have been particularly designed for use in the VoF solvers, both
incompressible and compressible.  Currently constant and temperature dependent
surface tension models are provided but it easy to write models in which the
surface tension is evaluated from any fields held by the mesh database.
2017-03-31 14:32:38 +01:00
cb1faea3f4 surfaceFilmModels::contactAngleForce: Added temperatureDependentContactAngleForce
Created a base-class from contactAngleForce from which the
distributionContactAngleForce (for backward compatibility) and the new
temperatureDependentContactAngleForce are derived:

Description
    Temperature dependent contact angle force

    The contact angle in degrees is specified as a \c Function1 type, to
    enable the use of, e.g.  contant, polynomial, table values.

See also
    Foam::regionModels::surfaceFilmModels::contactAngleForce
    Foam::Function1Types

SourceFiles
    temperatureDependentContactAngleForce.C
2017-03-27 20:03:28 +01:00
81ee0951b4 reactingTwoPhaseEulerFoam: Small change to avoid warning from wmkdep 2017-03-24 17:27:43 +00:00
2da9c7f2b5 Merge branch 'master' of github.com-OpenFOAM:OpenFOAM/OpenFOAM-dev 2017-03-18 17:19:35 +00:00
a166237d08 reactingMultiphaseEulerFoam: Ensure that an unordered phase pair gets
generated whenever a BlendedInterfacialModel is created.

Resolves bug-report https://bugs.openfoam.org/view.php?id=2472
2017-03-17 11:29:15 +00:00
ac41194341 reactingEulerFoam: Added fvOption support for incompressible phases 2017-03-14 11:56:01 +00:00
13aacde1c7 interFoam family of solvers: Improved Crank-Nicolson implementation
Fewer limiter iterations are now required to obtain sufficient boundedness and
restart is more consistent.
2017-03-06 17:34:10 +00:00
5bc07189ee reactingTwoPhaseEulerFoam::Lavieville: Corrected fLiquid function
Resolves bug-report https://bugs.openfoam.org/view.php?id=2477
2017-02-27 09:39:46 +00:00
80123f59ce thermophysicalProperties: New base-class for liquidProperties and in the future gasProperties
Description
    Base-class for thermophysical properties of solids, liquids and gases
    providing an interface compatible with the templated thermodynamics
    packages.

liquidProperties, solidProperties and thermophysicalFunction libraries have been
combined with the new thermophysicalProperties class into a single
thermophysicalProperties library to simplify compilation and linkage of models,
libraries and applications dependent on these classes.
2017-02-18 21:53:20 +00:00
abc50e214c thermophysicalModels: Changed specie thermodynamics from mole to mass basis
The fundamental properties provided by the specie class hierarchy were
mole-based, i.e. provide the properties per mole whereas the fundamental
properties provided by the liquidProperties and solidProperties classes are
mass-based, i.e. per unit mass.  This inconsistency made it impossible to
instantiate the thermodynamics packages (rhoThermo, psiThermo) used by the FV
transport solvers on liquidProperties.  In order to combine VoF with film and/or
Lagrangian models it is essential that the physical propertied of the three
representations of the liquid are consistent which means that it is necessary to
instantiate the thermodynamics packages on liquidProperties.  This requires
either liquidProperties to be rewritten mole-based or the specie classes to be
rewritten mass-based.  Given that most of OpenFOAM solvers operate
mass-based (solve for mass-fractions and provide mass-fractions to sub-models it
is more consistent and efficient if the low-level thermodynamics is also
mass-based.

This commit includes all of the changes necessary for all of the thermodynamics
in OpenFOAM to operate mass-based and supports the instantiation of
thermodynamics packages on liquidProperties.

Note that most users, developers and contributors to OpenFOAM will not notice
any difference in the operation of the code except that the confusing

    nMoles     1;

entries in the thermophysicalProperties files are no longer needed or used and
have been removed in this commet.  The only substantial change to the internals
is that species thermodynamics are now "mixed" with mass rather than mole
fractions.  This is more convenient except for defining reaction equilibrium
thermodynamics for which the molar rather than mass composition is usually know.
The consequence of this can be seen in the adiabaticFlameT, equilibriumCO and
equilibriumFlameT utilities in which the species thermodynamics are
pre-multiplied by their molecular mass to effectively convert them to mole-basis
to simplify the definition of the reaction equilibrium thermodynamics, e.g. in
equilibriumCO

    // Reactants (mole-based)
    thermo FUEL(thermoData.subDict(fuelName)); FUEL *= FUEL.W();

    // Oxidant (mole-based)
    thermo O2(thermoData.subDict("O2")); O2 *= O2.W();
    thermo N2(thermoData.subDict("N2")); N2 *= N2.W();

    // Intermediates (mole-based)
    thermo H2(thermoData.subDict("H2")); H2 *= H2.W();

    // Products (mole-based)
    thermo CO2(thermoData.subDict("CO2")); CO2 *= CO2.W();
    thermo H2O(thermoData.subDict("H2O")); H2O *= H2O.W();
    thermo CO(thermoData.subDict("CO")); CO *= CO.W();

    // Product dissociation reactions

    thermo CO2BreakUp
    (
        CO2 == CO + 0.5*O2
    );

    thermo H2OBreakUp
    (
        H2O == H2 + 0.5*O2
    );

Please report any problems with this substantial but necessary rewrite of the
thermodynamic at https://bugs.openfoam.org

Henry G. Weller
CFD Direct Ltd.
2017-02-17 11:22:14 +00:00
1c8a0bdcb3 compressibleInterFoam: Completed LTS and semi-implicit MULES support
Now the interFoam and compressibleInterFoam families of solvers use the same
alphaEqn formulation and supporting all of the MULES options without
code-duplication.

The semi-implicit MULES support allows running with significantly larger
time-steps but this does reduce the interface sharpness.
2017-02-09 17:31:57 +00:00
1aec2695f1 compressibleInterFoam: More consistent with interFoam and added partial support for LTS 2017-02-08 20:50:07 +00:00
11e298382e interFoam, interDyMFoam: Removed duplicate include 2017-02-08 20:47:59 +00:00
e5b5a34014 interMixingFoam: Renamed alphaEqns.H and alphaEqnsSubCycle.H for consistency with interFoam 2017-02-08 20:46:31 +00:00