Commit Graph

1636 Commits

Author SHA1 Message Date
a752d3e588 saturationModels: Added Tsat function
Currently this is implemented only for the Antoine equation, for the
other more complex models an iterative inversion from pressure to
temperature is required.
2015-07-04 14:46:55 +01:00
7c6e1386f1 reactingTwoPhaseEulerFoam: Completed mass-transfer terms in both forms of momentum equations 2015-07-03 23:18:25 +01:00
9c9ac368fe reactingTwoPhaseEulerFoam: Replace x*pos(x) with posPart(x) and same for neg 2015-07-03 18:04:34 +01:00
2ee2a52fff reactingTwoPhaseEulerFoam: Updated wmake files 2015-07-03 17:44:34 +01:00
243accc6f6 reactingTwoPhaseEulerFoam: Renamed saturationPressureModel -> saturationModel
In preparation for adding the Tsat function
2015-07-03 16:15:09 +01:00
08682ca3eb Removed temporary Info statement 2015-07-03 15:47:25 +01:00
a92691b0dd reactingTwoPhaseEulerFoam: Added mass-exchange contribution to the cell-based momentum equations 2015-07-03 15:46:52 +01:00
b0d107499b reactingTwoPhaseEulerFoam: Changed the handling of the energy transfer
for consistency with the evaluation of the interface temperature.
2015-07-03 15:45:56 +01:00
68ea75a37c reactingTwoPhaseEulerFoam: Corrected handling of heat-transfer caused by mass-transfer 2015-07-02 22:51:06 +01:00
be16ebf24f reactingTwoPhaseEulerFoam/pU/pEqn: Added missing dmdt terms 2015-07-02 22:50:44 +01:00
d0f15d4e3c EEqn: Added rho*(U&g) source term
Generally this term has a VERY small effect on temperature, it is only
important for low-speed buoyancy-dominated flows.

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1755

See also http://cfd.direct/openfoam/energy-equation/
2015-07-01 10:53:37 +01:00
1f7b3883ff pimpleFoam: Caching 1/A is no longer necessary 2015-06-30 16:07:42 +01:00
8b47981d3e pisoFoam: Added MRF and fvOptions support 2015-06-30 15:21:00 +01:00
aa42c1f906 kOmegaSSTSato: Relocated to src/TurbulenceModels/phaseCompressible/RAS 2015-06-30 13:04:27 +01:00
fd9d07413a LTS: Simplify the selection of LTS operation 2015-06-29 11:53:20 +01:00
f92d657ab7 LTS: Formalize the naming of the rDeltaT and rSubDeltaT fields
Now the specification of the LTS time scheme is simply:

ddtSchemes
{
    default         localEuler;
}
2015-06-28 21:41:40 +01:00
af8185c0a6 reactingParcelFoam, coalChemistryFoam: Added LTS support
Replaces LTSReactingParcelFoam and LTSCoalChemistryFoam

    Select LTS via the ddtScheme:

        ddtSchemes
        {
            default         localEuler rDeltaT;
        }
2015-06-28 11:01:04 +01:00
01cb591ba5 rhoReactingFoam, rhoReactingBuoyantFoam: Added LTS support
Select LTS via the ddtScheme:

    ddtSchemes
    {
        default         localEuler rDeltaT;
    }
2015-06-27 22:41:00 +01:00
64e831fea0 reactingFoam: Added run-time selectable LTS support replacing LTSReactingFoam
Select LTS via the ddtScheme:

    ddtSchemes
    {
        default         localEuler rDeltaT;
    }
2015-06-27 22:35:49 +01:00
4180b6857d rhoPimpleFoam: Added run-time selectable LTS support replacing rhoLTSPimpleFoam
Select LTS via the ddtScheme:

        ddtSchemes
        {
            default         localEuler rDeltaT;
        }
2015-06-27 22:08:43 +01:00
60cffb2fc3 pimpleFoam family: Added PIMPLEC (PIMPLE-consistent) support
Select using the optional

    consistent true;

setting in the PIMPLE dictionary of fvSolution.

This option is generally only beneficial for cases run in PIMPLE-mode
with a large maximum Courant number.
2015-06-27 18:56:24 +01:00
8fc3d158ff rhoSimpleFoam: Added "consistent" option to replace rhoSimplecFoam
See tutorials/compressible/rhoSimpleFoam/squareBend

SIMPLE
{
    nNonOrthogonalCorrectors 0;
    rhoMin          0.1;
    rhoMax          1.0;
    transonic       yes;
    consistent      yes;

    residualControl
    {
        p               1e-3;
        U               1e-4;
        e               1e-3;

        // possibly check turbulence fields
        "(k|epsilon|omega)" 1e-3;
    }
}

relaxationFactors
{
    fields
    {
        p               1;
        rho             1;
    }
    equations
    {
        p               1;
        U               0.9;
        e               0.9;
        k               0.9;
        epsilon         0.9;
    }
}
2015-06-27 17:42:59 +01:00
8cad93c724 rhoPimpleFoam: Added "consistent" option to replace rhoPimplecFoam
e.g. in tutorials/compressible/rhoPimpleFoam/ras/angledDuctLTS

PIMPLE
{
    momentumPredictor   yes;
    transonic           no;
    nOuterCorrectors    50;
    nCorrectors         1;
    nNonOrthogonalCorrectors 0;
    consistent          yes;

    rhoMin          0.5;
    rhoMax          2.0;

    residualControl
    {
        "(U|k|epsilon)"
        {
            relTol          0;
            tolerance       0.0001;
        }
    }

    turbOnFinalIterOnly off;
}

relaxationFactors
{
    fields
    {
        "p.*"           0.9;
        "rho.*"         1;
    }
    equations
    {
        "U.*"           0.9;
        "h.*"           0.7;
        "(k|epsilon|omega).*" 0.8;
    }
}
2015-06-27 16:26:51 +01:00
5c4b7b1640 Rename setrDeltaT to setRDeltaT 2015-06-27 15:33:39 +01:00
a9fa0db19a Rename setrDeltaT to setRDeltaT 2015-06-27 15:33:04 +01:00
ca81d01ca8 LTSReactingParcelFoam: Minor improvement 2015-06-27 12:30:10 +01:00
edcc472535 reactingTwoPhaseEulerFoam: Removed superfluous trSubDeltaT field 2015-06-26 22:05:39 +01:00
587c93574a LTS, MULES and sub-cycling: Improved the handling of the rSubDeltaT field 2015-06-26 21:58:27 +01:00
d14e8ed169 interFoam: Change construction order 2015-06-26 18:54:37 +01:00
1d16db3fa0 reactingTwoPhaseEulerFoam: Added experimental run-time selectable LTS support
Select LTS via the ddtScheme:

    ddtSchemes
    {
        default         localEuler rDeltaT;
    }

The LTS algorithm is currently controlled with the standard settings in
controlDict, e.g.:

    maxCo           0.5;
    maxDeltaT       2e-8;

with the addition of the optional rDeltaT smoothing coefficient:

    rDeltaTSmoothingCoeff 0.02;

which defaults to 0.02.

    ddtSchemes
    {
        default         localEuler rDeltaT;
    }
2015-06-26 18:52:23 +01:00
e00ae44ad0 interFoam family: Added run-time selectable LTS support
LTS is selected by the ddt scheme e.g. in the
tutorials/multiphase/interFoam/ras/DTCHull case:

ddtSchemes
{
    default         localEuler rDeltaT;
}

LTSInterFoam is no longer needed now that interFoam includes LTS
support.
2015-06-26 18:32:20 +01:00
bf95b5c286 reactingTwoPhaseEulerFoam: Change the implicit handling of phase-pressure and dispersion
to support any number of phases
2015-06-26 15:15:10 +01:00
4d6823c3eb reactingTwoPhaseEulerFoam: Minor reorganization 2015-06-25 22:43:22 +01:00
5d3d40392f reactingTwoPhaseEulerFoam: Add fvOption handling to the continuity error
correction in MovingPhaseModel<BasePhaseModel>::correct()
2015-06-25 22:29:08 +01:00
e9ecd7ddef twoPhaseEulerFoam, reactingTwoPhaseEulerFoam: Removed duplicate files 2015-06-25 20:27:09 +01:00
5ebf61eb41 smoluchowskiJumpTFvPatchScalarField: Updated use of basicThermo 2015-06-25 19:28:16 +01:00
0f8d7e677d reactingTwoPhaseEulerFoam: Construct MRF and fvOptions in phaseSystem 2015-06-25 19:22:47 +01:00
550ba440fd reactingTwoPhaseEulerFoam: Change the sign of the compressibility correction field
to correspond to the phase dilatation rate.
2015-06-25 16:37:53 +01:00
9f6c161e49 reactingTwoPhaseEulerFoam: Generalize the handling of the dilatation rate
to support any number of phases
2015-06-25 16:10:07 +01:00
69d994e794 twoPhaseEulerFoam: Change the implicit particle-pressure and turbulence dispersion
to be phase-symmetric so that the results are independent of which
phase-fraction is solved.
2015-06-25 16:08:21 +01:00
ad40e110df Update headers 2015-06-24 10:45:42 +01:00
5e05479e2a Use basicThermo::dictName rather than hard-coding "thermophysicalProperties" 2015-06-24 10:44:57 +01:00
e332c4a335 simpleFoam: Construct a turbulenceModel rather than RASModel
to support laminar simulations in the new framework.

Unfortunately this allows LES models to be instantiated although they
are not compatible with steady-state simulations.
2015-06-23 10:52:45 +01:00
91ee15e3ac rhoCentralFoam: Added experimental LTS support
Select LTS via the ddtScheme:

ddtSchemes
{
    default         localEuler rDeltaT;
}

The LTS algorithm is controlled with the standard settings in
controlDict, e.g.:

maxCo           0.5;
maxDeltaT       2e-8;

with the addition of the optional rDeltaT smoothing coefficient:

rDeltaTSmoothingCoeff 0.02;

which defaults to 0.02.

For cases with reasonably uniform meshes like the forwardStep tutorial
LTS does not provide much benefit but for cases with large variation in
cell-size like the biconic25-55Run35 tutorial LTS provides significant
speed-up to convergence particularly if started from uniform conditions.
2015-06-19 11:52:48 +01:00
80e13f8002 rhoCentralFoam: Reverted correction to BCs
Reverted changes proposed in
http://openfoam.org/mantisbt/view.php?id=1548 as it adversely affects
fixed-value BCs and is formulated to fix an issue with an unphysical
case.  Further analysis of the handling of fixed pressure outlet
conditions as the Mach number approaches 1 is required.
2015-06-18 15:10:48 +01:00
164448f8b1 rhoCentralFoam: Updated Courant number calculation to be cell-based rather than face-based
Now consistent with the way the Courant number is calculated for other solvers
2015-06-17 20:20:49 +01:00
bc493180d9 rhoCentralFoam: Ensure fixed value boundary conditions are preserved
Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1748
2015-06-17 08:46:46 +01:00
8293227964 Rationalized the LTS solvers 2015-06-16 12:42:37 +01:00
03adb37ab4 LTSCoalChemistryFoam: LTS version of coalChemistryFoam 2015-06-15 22:36:27 +01:00
eb53f9bdf0 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