Commit graph

10 commits

Author SHA1 Message Date
Henry Weller
dbb428a3a8 Updated to OpenFOAM-5.x 2017-07-25 14:23:49 +01:00
Henry Weller
e3c67dc111 fvOptions: The "<type>Coeffs" sub-dictionary is now optional
For example the actuationDiskSource fvOption may now be specified

disk1
{
    type            actuationDiskSource;

    fields      (U);

    selectionMode   cellSet;
    cellSet         actuationDisk1;
    diskDir         (1 0 0);    // Orientation of the disk
    Cp              0.386;
    Ct              0.58;
    diskArea        40;
    upstreamPoint   (581849 4785810 1065);
}

rather than

disk1
{
    type            actuationDiskSource;
    active          on;

    actuationDiskSourceCoeffs
    {
        fields      (U);

        selectionMode   cellSet;
        cellSet         actuationDisk1;
        diskDir         (1 0 0);    // Orientation of the disk
        Cp              0.386;
        Ct              0.58;
        diskArea        40;
        upstreamPoint   (581849 4785810 1065);
    }
}

but this form is supported for backward compatibility.
2017-04-13 13:30:17 +01:00
Henry Weller
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
Chris Greenshields
a1cc51b116 Tutorials fvSolution files: removed solver entries which use default
values; formatted Switch entries consistently across all cases
2016-06-15 07:39:37 +01:00
Henry Weller
8cdd590333 tutorials: Renamed .org -> .orig
See http://www.openfoam.org/mantisbt/view.php?id=2076
  - .org is the file extension for emacs org-mode as well
  - .orig is more to the point (.org isn't always recognized as "original")
  - .original is too long, although more consistent with the convention
    of source code file naming

Update script contributed by Bruno Santos
2016-04-30 21:53:50 +01:00
Henry Weller
d0e45416e0 tutorials: Removed unnecessary "boundary" files 2015-11-13 20:05:37 +00:00
Henry Weller
ecee2d275e Input of dimensionedScalars: update read-construction of dimensionedScalar in applications
so that the specification of the name and dimensions are optional in property dictionaries.

Update tutorials so that the name of the dimensionedScalar property is
no longer duplicated but optional dimensions are still provided and are
checked on read.
2015-07-20 22:52:53 +01:00
Henry Weller
dc0523643f fluxRequired: Added setFluxRequired function to fvSchemes class
Added calls to setFluxRequired for p, p_rgh etc. in all solvers which
avoids the need to add fluxRequired entries in fvSchemes dictionaries.
2015-07-15 21:57:16 +01:00
Henry Weller
6f53722dab tutorials/multiphase/.*woPhaseEulerFoam/: Change outlet p_rgh BC to prghPressure 2015-06-29 19:36:57 +01:00
Henry Weller
3ed90ae73d reactingTwoPhaseEulerFoam: New twoPhaseEulerFoam supporting mass-transfer and reactions
Multi-species, mass-transfer and reaction support and multi-phase
structure provided by William Bainbridge.

Integration of the latest p-U and face-p_U algorithms with William's
multi-phase structure is not quite complete due to design
incompatibilities which needs further development.  However the
integration of the functionality is complete.

The results of the tutorials are not exactly the same for the
twoPhaseEulerFoam and reactingTwoPhaseEulerFoam solvers but are very
similar.  Further analysis in needed to ensure these differences are
physical or to resolve them; in the meantime the twoPhaseEulerFoam
solver will be maintained.
2015-06-12 09:52:17 +01:00