Commit Graph

27 Commits

Author SHA1 Message Date
Andrew Heather
79e353b84e RELEASE: Updated version to v2012 2020-12-23 10:01:39 +01:00
Andrew Heather
538d749220 REL: Updated headers to version v2006 2020-06-29 17:27:54 +01:00
Andrew Heather
ae2ab06312 REL: Release preparations 2019-12-23 09:49:23 +00:00
Andrew Heather
be44dcaf1f RELEASE: Version clean-up for release 2019-06-25 11:51:19 +01:00
Sergio Ferraris
8170f2ad92 INT: Org integration of VOF, Euler phase solvers and models.
Integration of VOF MULES new interfaces. Update of VOF solvers and all instances
of MULES in the code.
Integration of reactingTwoPhaseEuler and reactingMultiphaseEuler solvers and sub-models
Updating reactingEuler tutorials accordingly (most of them tested)

New eRefConst thermo used in tutorials. Some modifications at thermo specie level
affecting mostly eThermo. hThermo mostly unaffected

New chtMultiRegionTwoPhaseEulerFoam solver for quenching and tutorial.

Phases sub-models for reactingTwoPhaseEuler and reactingMultiphaseEuler were moved
to src/phaseSystemModels/reactingEulerFoam in order to be used by BC for
chtMultiRegionTwoPhaseEulerFoam.

Update of interCondensatingEvaporatingFoam solver.
2019-06-07 09:38:35 +01:00
Andrew Heather
9231534efa STYLE: Updating version to v1812 2018-12-19 18:07:52 +00:00
Andrew Heather
6e35bcda70 ENH: Updated config for release v1806 2018-06-28 12:56:00 +01:00
Andrew Heather
dcb1a95e35 MRG: Integrated Foundation code to commit 7d6845d 2017-03-23 14:33:33 +00:00
Henry Weller
c52e4b58a1 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
Andrew Heather
f0c3e8d599 STYLE: Updated version to 'plus' 2015-12-22 23:14:17 +00:00
Andrew Heather
0e01c44129 GIT: Resolved conflict 2015-12-09 16:19:28 +00:00
Andrew Heather
8837a89237 STYLE: Updated links from openfoam.org to openfoam.com 2015-12-09 15:03:05 +00:00
Henry Weller
d98136e122 tutorials: Removed unnecessary "boundary" files 2015-11-13 20:05:37 +00:00
Henry
61e52b2cb4 twoPhaseEulerFoam: Move the residualAlpha used for drag into the phaseModel
This is necessary to guarantee consistency between the residualAlpha
used for drag and buoyancy in a multi-phase system
2015-06-07 18:55:24 +01:00
Henry
50ada7c994 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
OpenFOAM-admin
9fb26d59d3 GIT: Repo update 2014-12-11 08:35:10 +00:00
Henry
85da9e6a54 twoPhaseEulerFoam: Now in fully-conservative form 2014-04-29 15:47:39 +01:00
william
37c75a8b18 BUG: twoPhaseEulerFoam: removed multiple of the continuous phase fraction from force and heat transfer models 2014-03-17 16:34:32 +00:00
OpenFOAM-admin
fbb3ddf2c4 Updated for release 2.3.0 2014-02-17 10:21:46 +00:00
william
05a34f3dfa ENH: twoPhaseEulerFoam: changed Cd function to CdRe and removed some residual constants 2014-02-03 12:51:59 +00:00
william
87115af2d0 ENH: twoPhaseEulerFoam: Removed requirement that a model (most likely "none") had to be specified for all pairs 2014-01-23 16:37:16 +00:00
william
acf490cb44 STYLE: twoPhaseEulerFoam: updated tutorials for bubble library developments 2014-01-23 11:27:37 +00:00
william
5d55a1f60f ENH: Added noLift model for twoPhaseEulerFoam 2014-01-06 14:16:41 +00:00
william
475e885772 ENH: Abstracted and made run-time selectable the lift models in twoPhaseEulerFoam 2014-01-02 16:53:37 +00:00
andy
d302bf6819 STYLE: Updated spelling errors 2013-11-26 14:45:27 +00:00
Henry
79467c20ae twoPhaseEulerFoam: Added IATE 2013-10-10 16:29:21 +01:00
Henry
175f03f87d Removed twoPhaseEulerFoam and renamed compressibleTwoPhaseEulerFoam -> twoPhaseEulerFoam 2013-08-15 10:30:09 +01:00