Commit Graph

9 Commits

Author SHA1 Message Date
15a2e7f6e9 combustionModel, chemistryModel: Simplified model selection
Updated all tutorials to the new format
2017-12-11 15:20:47 +00:00
95574a6c6b liquidProperties, solidProperties: Simplified input
The entries for liquid and solid species can now be simply be the name unless
property coefficients are overridden in which are specified in a dictionary as
before e.g. in the tutorials/lagrangian/coalChemistryFoam/simplifiedSiwek case
the water is simply specified

liquids
{
    H2O;
}

and solid ash uses standard coefficients but the coefficients for carbon are
overridden thus

solids
{
    C
    {
        rho             2010;
        Cp              710;
        kappa           0.04;
        Hf              0;
        emissivity      1.0;
    }

    ash;
}
2017-02-18 12:43:10 +00:00
081f1784f9 liquidProperties: Simplified dictionary format
The defaultCoeffs entry is now redundant and supported only for backward
compatibility.  To specify a liquid with default coefficients simply leave the
coefficients dictionary empty:

    liquids
    {
        H2O {}
    }

Any or all of the coefficients may be overridden by specifying the properties in
the coefficients dictionary, e.g.

    liquids
    {
        H2O
        {
            rho
            {
                a 1000;
                b 0;
                c 0;
                d 0;
            }
        }
    }
2017-02-17 22:08:42 +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
6f338ed716 PaSR: Removed deprecated "turbulentReaction" switch
To run with laminar reaction rates choose the "laminar" combustion model rather
than setting "turbulentReaction no;" in the "PaSR" model.
2017-01-20 17:17:14 +00:00
d0e45416e0 tutorials: Removed unnecessary "boundary" files 2015-11-13 20:05:37 +00:00
2b1ee6b497 tutorials: Removed unnecessary spaces between parentheses and values in vectors 2015-07-21 20:55:44 +01:00
3a3c29b284 blockMesh: Change default location of blockMeshDict from constant/polyMesh to system
For multi-region cases the default location of blockMeshDict is now system/<region name>

If the blockMeshDict is not found in system then the constant directory
is also checked providing backward-compatibility
2015-04-24 22:29:57 +01:00
446e5777f0 Add the OpenFOAM source tree 2014-12-10 22:40:10 +00:00