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ENH: deprecated dieselSpray library and related solvers/deps
This commit is contained in:
andy
@ -1,3 +0,0 @@
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dieselEngineFoam.C
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EXE = $(FOAM_APPBIN)/dieselEngineFoam
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@ -1,40 +0,0 @@
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EXE_INC = \
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-I../engineFoam \
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-I$(LIB_SRC)/turbulenceModels/compressible/turbulenceModel \
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-I$(LIB_SRC)/lagrangian/basic/lnInclude \
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-I$(LIB_SRC)/meshTools/lnInclude \
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-I$(LIB_SRC)/lagrangian/dieselSpray/lnInclude \
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-I$(LIB_SRC)/thermophysicalModels/properties/liquidProperties/lnInclude \
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-I$(LIB_SRC)/thermophysicalModels/properties/liquidMixtureProperties/lnInclude \
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-I$(LIB_SRC)/thermophysicalModels/specie/lnInclude \
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-I$(LIB_SRC)/thermophysicalModels/thermophysicalFunctions/lnInclude \
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-I$(LIB_SRC)/thermophysicalModels/reactionThermo/lnInclude \
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-I$(LIB_SRC)/thermophysicalModels/basic/lnInclude \
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-I$(LIB_SRC)/thermophysicalModels/laminarFlameSpeed/lnInclude \
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-I$(LIB_SRC)/../applications/solvers/reactionThermo/XiFoam \
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-I$(LIB_SRC)/thermophysicalModels/chemistryModel/lnInclude \
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-I$(LIB_SRC)/ODE/lnInclude \
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-I$(LIB_SRC)/engine/lnInclude \
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-I$(LIB_SRC)/finiteVolume/lnInclude \
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-I$(LIB_SRC)/combustionModels/lnInclude
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EXE_LIBS = \
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-lengine \
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-lcompressibleTurbulenceModel \
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-lcompressibleRASModels \
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-lcompressibleLESModels \
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-lreactionThermophysicalModels \
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-lfiniteVolume \
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-llagrangian \
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-lmeshTools \
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-ldieselSpray \
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-lliquidProperties \
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-lliquidMixtureProperties \
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-lthermophysicalFunctions \
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-lspecie \
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-lbasicThermophysicalModels \
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-llaminarFlameSpeedModels \
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-lchemistryModel \
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-lODE \
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-ldistributionModels \
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-lcombustionModels
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@ -1,14 +0,0 @@
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fvVectorMatrix UEqn
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(
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fvm::ddt(rho, U)
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+ fvm::div(phi, U)
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+ turbulence->divDevRhoReff(U)
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==
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rho*g
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+ dieselSpray.momentumSource()
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);
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if (pimple.momentumPredictor())
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{
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solve(UEqn == -fvc::grad(p));
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}
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@ -1,48 +0,0 @@
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tmp<fv::convectionScheme<scalar> > mvConvection
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(
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fv::convectionScheme<scalar>::New
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(
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mesh,
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fields,
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phi,
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mesh.divScheme("div(phi,Yi_h)")
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)
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);
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{
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combustion->correct();
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dQ = combustion->dQ();
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label inertIndex = -1;
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volScalarField Yt(0.0*Y[0]);
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forAll(Y, i)
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{
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if (Y[i].name() != inertSpecie)
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{
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volScalarField& Yi = Y[i];
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fvScalarMatrix YiEqn
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(
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fvm::ddt(rho, Yi)
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+ mvConvection->fvmDiv(phi, Yi)
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- fvm::laplacian(turbulence->muEff(), Yi)
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==
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dieselSpray.evaporationSource(i)
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+ combustion->R(Yi)
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);
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YiEqn.relax();
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YiEqn.solve(mesh.solver("Yi"));
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Yi.max(0.0);
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Yt += Yi;
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}
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else
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{
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inertIndex = i;
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}
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}
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Y[inertIndex] = scalar(1) - Yt;
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Y[inertIndex].max(0.0);
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}
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@ -1,104 +0,0 @@
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Info<< "Creating combustion model\n" << endl;
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autoPtr<combustionModels::psiChemistryCombustionModel> combustion
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(
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combustionModels::psiChemistryCombustionModel::New
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(
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mesh
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)
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);
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psiChemistryModel& chemistry = combustion->pChemistry();
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hsCombustionThermo& thermo = chemistry.thermo();
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basicMultiComponentMixture& composition = thermo.composition();
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PtrList<volScalarField>& Y = composition.Y();
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word inertSpecie(thermo.lookup("inertSpecie"));
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if (!composition.contains(inertSpecie))
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{
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FatalErrorIn(args.executable())
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<< "Specified inert specie '" << inertSpecie << "' not found in "
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<< "species list. Available species:" << composition.species()
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<< exit(FatalError);
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}
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volScalarField rho
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(
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IOobject
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(
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"rho",
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runTime.timeName(),
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mesh
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),
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thermo.rho()
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);
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Info<< "Reading field U\n" << endl;
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volVectorField U
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(
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IOobject
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(
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"U",
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runTime.timeName(),
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mesh,
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IOobject::MUST_READ,
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IOobject::AUTO_WRITE
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),
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mesh
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);
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volScalarField& p = thermo.p();
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const volScalarField& psi = thermo.psi();
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const volScalarField& T = thermo.T();
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volScalarField& hs = thermo.hs();
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#include "compressibleCreatePhi.H"
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Info << "Creating turbulence model.\n" << nl;
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autoPtr<compressible::turbulenceModel> turbulence
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(
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compressible::turbulenceModel::New
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(
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rho,
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U,
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phi,
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thermo
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)
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);
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// Set the turbulence into the combustion model
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combustion->setTurbulence(turbulence());
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Info<< "Creating field DpDt\n" << endl;
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volScalarField DpDt
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(
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fvc::DDt(surfaceScalarField("phiU", phi/fvc::interpolate(rho)), p)
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);
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multivariateSurfaceInterpolationScheme<scalar>::fieldTable fields;
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forAll(Y, i)
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{
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fields.add(Y[i]);
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}
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fields.add(hs);
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volScalarField dQ
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(
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IOobject
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(
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"dQ",
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runTime.timeName(),
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mesh,
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IOobject::NO_READ,
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IOobject::AUTO_WRITE
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),
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mesh,
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dimensionedScalar("dQ", dimEnergy/dimTime, 0.0)
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);
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@ -1,37 +0,0 @@
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Info << "Constructing Spray" << endl;
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PtrList<gasThermoPhysics> gasProperties(Y.size());
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forAll(gasProperties, i)
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{
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gasProperties.set
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(
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i,
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new gasThermoPhysics
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(
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dynamic_cast<const reactingMixture<gasThermoPhysics>&>
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(thermo).speciesData()[i]
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)
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);
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}
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spray dieselSpray
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(
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U,
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rho,
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p,
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T,
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composition,
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gasProperties,
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thermo,
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g
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);
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scalar gasMass0 = fvc::domainIntegrate(rho).value();
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if (dieselSpray.twoD())
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{
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gasMass0 *= constant::mathematical::twoPi/dieselSpray.angleOfWedge();
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}
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gasMass0 -=
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dieselSpray.injectedMass(runTime.value()) - dieselSpray.liquidMass();
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@ -1,122 +0,0 @@
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/*---------------------------------------------------------------------------*\
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========= |
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
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\\ / O peration |
|
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\\ / A nd | Copyright (C) 2011 OpenFOAM Foundation
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\\/ M anipulation |
|
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-------------------------------------------------------------------------------
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License
|
||||
This file is part of OpenFOAM.
|
||||
|
||||
OpenFOAM is free software: you can redistribute it and/or modify it
|
||||
under the terms of the GNU General Public License as published by
|
||||
the Free Software Foundation, either version 3 of the License, or
|
||||
(at your option) any later version.
|
||||
|
||||
OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
|
||||
ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
|
||||
FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
|
||||
for more details.
|
||||
|
||||
You should have received a copy of the GNU General Public License
|
||||
along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
|
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Application
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dieselEngineFoam
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Description
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Solver for diesel engine spray and combustion.
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\*---------------------------------------------------------------------------*/
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#include "fvCFD.H"
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#include "engineTime.H"
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#include "engineMesh.H"
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#include "turbulenceModel.H"
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#include "psiChemistryCombustionModel.H"
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#include "spray.H"
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#include "psiChemistryModel.H"
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#include "chemistrySolver.H"
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#include "multivariateScheme.H"
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#include "Switch.H"
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#include "OFstream.H"
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#include "volPointInterpolation.H"
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#include "thermoPhysicsTypes.H"
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#include "mathematicalConstants.H"
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#include "pimpleControl.H"
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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int main(int argc, char *argv[])
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{
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#include "setRootCase.H"
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#include "createEngineTime.H"
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#include "createEngineMesh.H"
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#include "createFields.H"
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#include "readGravitationalAcceleration.H"
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#include "createSpray.H"
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#include "initContinuityErrs.H"
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#include "readEngineTimeControls.H"
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#include "compressibleCourantNo.H"
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#include "setInitialDeltaT.H"
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#include "startSummary.H"
|
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|
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pimpleControl pimple(mesh);
|
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|
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
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Info<< "\nStarting time loop\n" << endl;
|
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while (runTime.run())
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{
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#include "readEngineTimeControls.H"
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#include "compressibleCourantNo.H"
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#include "setDeltaT.H"
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runTime++;
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Info<< "Crank angle = " << runTime.theta() << " CA-deg" << endl;
|
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|
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mesh.move();
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|
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dieselSpray.evolve();
|
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#include "rhoEqn.H"
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||||
|
||||
while (pimple.loop())
|
||||
{
|
||||
#include "UEqn.H"
|
||||
#include "YEqn.H"
|
||||
#include "hsEqn.H"
|
||||
|
||||
// --- Pressure corrector loop
|
||||
while (pimple.correct())
|
||||
{
|
||||
#include "pEqn.H"
|
||||
}
|
||||
|
||||
if (pimple.turbCorr())
|
||||
{
|
||||
turbulence->correct();
|
||||
}
|
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}
|
||||
|
||||
#include "logSummary.H"
|
||||
#include "spraySummary.H"
|
||||
|
||||
rho = thermo.rho();
|
||||
|
||||
runTime.write();
|
||||
|
||||
Info<< "ExecutionTime = " << runTime.elapsedCpuTime() << " s"
|
||||
<< " ClockTime = " << runTime.elapsedClockTime() << " s"
|
||||
<< nl << endl;
|
||||
}
|
||||
|
||||
Info<< "End\n" << endl;
|
||||
|
||||
return 0;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -1,21 +0,0 @@
|
||||
{
|
||||
fvScalarMatrix hsEqn
|
||||
(
|
||||
fvm::ddt(rho, hs)
|
||||
+ mvConvection->fvmDiv(phi, hs)
|
||||
- fvm::laplacian(turbulence->alphaEff(), hs)
|
||||
==
|
||||
DpDt
|
||||
+ combustion->Sh()
|
||||
+ dieselSpray.heatTransferSource()()
|
||||
|
||||
);
|
||||
|
||||
hsEqn.relax();
|
||||
hsEqn.solve();
|
||||
|
||||
thermo.correct();
|
||||
|
||||
Info<< "min/max(T) = "
|
||||
<< min(T).value() << ", " << max(T).value() << endl;
|
||||
}
|
||||
@ -1,12 +0,0 @@
|
||||
Info<< "Mean pressure:" << p.weightedAverage(mesh.V()).value() << endl;
|
||||
Info<< "Mean temperature:" << T.weightedAverage(mesh.V()).value() << endl;
|
||||
Info<< "Mean u':"
|
||||
<< (sqrt((2.0/3.0)*turbulence->k()))().weightedAverage(mesh.V()).value()
|
||||
<< endl;
|
||||
|
||||
logSummaryFile
|
||||
<< runTime.theta() << tab
|
||||
<< p.weightedAverage(mesh.V()).value() << tab
|
||||
<< T.weightedAverage(mesh.V()).value() << tab
|
||||
<< (sqrt((2.0/3.0)*turbulence->k()))().weightedAverage(mesh.V()).value()
|
||||
<< endl;
|
||||
@ -1,65 +0,0 @@
|
||||
rho = thermo.rho();
|
||||
|
||||
volScalarField A(UEqn.A());
|
||||
U = UEqn.H()/A;
|
||||
|
||||
if (pimple.transonic())
|
||||
{
|
||||
surfaceScalarField phid
|
||||
(
|
||||
"phid",
|
||||
fvc::interpolate(psi)
|
||||
*((fvc::interpolate(U) & mesh.Sf()) - fvc::meshPhi(rho, U))
|
||||
);
|
||||
|
||||
while (pimple.correctNonOrthogonal())
|
||||
{
|
||||
fvScalarMatrix pEqn
|
||||
(
|
||||
fvm::ddt(psi, p)
|
||||
+ fvm::div(phid, p)
|
||||
- fvm::laplacian(rho/A, p)
|
||||
==
|
||||
Sevap
|
||||
);
|
||||
|
||||
pEqn.solve(mesh.solver(p.select(pimple.finalInnerIter())));
|
||||
|
||||
if (pimple.finalNonOrthogonalIter())
|
||||
{
|
||||
phi == pEqn.flux();
|
||||
}
|
||||
}
|
||||
}
|
||||
else
|
||||
{
|
||||
phi = fvc::interpolate(rho)
|
||||
*((fvc::interpolate(U) & mesh.Sf()) - fvc::meshPhi(rho, U));
|
||||
|
||||
while (pimple.correctNonOrthogonal())
|
||||
{
|
||||
fvScalarMatrix pEqn
|
||||
(
|
||||
fvm::ddt(psi, p)
|
||||
+ fvc::div(phi)
|
||||
- fvm::laplacian(rho/A, p)
|
||||
==
|
||||
Sevap
|
||||
);
|
||||
|
||||
pEqn.solve(mesh.solver(p.select(pimple.finalInnerIter())));
|
||||
|
||||
if (pimple.finalNonOrthogonalIter())
|
||||
{
|
||||
phi += pEqn.flux();
|
||||
}
|
||||
}
|
||||
}
|
||||
|
||||
#include "rhoEqn.H"
|
||||
#include "compressibleContinuityErrs.H"
|
||||
|
||||
U -= fvc::grad(p)/A;
|
||||
U.correctBoundaryConditions();
|
||||
|
||||
DpDt = fvc::DDt(surfaceScalarField("phiU", phi/fvc::interpolate(rho)), p);
|
||||
@ -1,64 +0,0 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011 OpenFOAM Foundation
|
||||
\\/ M anipulation |
|
||||
-------------------------------------------------------------------------------
|
||||
License
|
||||
This file is part of OpenFOAM.
|
||||
|
||||
OpenFOAM is free software: you can redistribute it and/or modify it
|
||||
under the terms of the GNU General Public License as published by
|
||||
the Free Software Foundation, either version 3 of the License, or
|
||||
(at your option) any later version.
|
||||
|
||||
OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
|
||||
ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
|
||||
FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
|
||||
for more details.
|
||||
|
||||
You should have received a copy of the GNU General Public License
|
||||
along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
|
||||
|
||||
Global
|
||||
rhoEqn
|
||||
|
||||
Description
|
||||
Solve the continuity for density.
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
volScalarField Sevap
|
||||
(
|
||||
IOobject
|
||||
(
|
||||
"Sevap",
|
||||
runTime.timeName(),
|
||||
mesh,
|
||||
IOobject::NO_READ,
|
||||
IOobject::NO_WRITE
|
||||
),
|
||||
mesh,
|
||||
dimensionedScalar("zero", dimensionSet(1, -3, -1, 0, 0), 0.0)
|
||||
);
|
||||
|
||||
forAll(Y, i)
|
||||
{
|
||||
if (dieselSpray.isLiquidFuel()[i])
|
||||
{
|
||||
Sevap += dieselSpray.evaporationSource(i);
|
||||
}
|
||||
}
|
||||
|
||||
{
|
||||
solve
|
||||
(
|
||||
fvm::ddt(rho)
|
||||
+ fvc::div(phi)
|
||||
==
|
||||
Sevap
|
||||
);
|
||||
}
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -1,30 +0,0 @@
|
||||
label Nparcels = dieselSpray.size();
|
||||
reduce(Nparcels, sumOp<label>());
|
||||
|
||||
Info<< "\nNumber of parcels in system.... | "
|
||||
<< Nparcels << endl
|
||||
<< "Injected liquid mass........... | "
|
||||
<< 1e6*dieselSpray.injectedMass(runTime.value()) << " mg" << endl
|
||||
<< "Liquid Mass in system.......... | "
|
||||
<< 1e6*dieselSpray.liquidMass() << " mg" << endl
|
||||
<< "SMD, Dmax...................... | "
|
||||
<< dieselSpray.smd()*1e6 << " mu, "
|
||||
<< dieselSpray.maxD()*1e6 << " mu"
|
||||
<< endl;
|
||||
|
||||
scalar evapMass =
|
||||
dieselSpray.injectedMass(runTime.value())
|
||||
- dieselSpray.liquidMass();
|
||||
|
||||
scalar gasMass = fvc::domainIntegrate(rho).value();
|
||||
|
||||
if (dieselSpray.twoD())
|
||||
{
|
||||
gasMass *= constant::mathematical::twoPi/dieselSpray.angleOfWedge();
|
||||
}
|
||||
|
||||
scalar addedMass = gasMass - gasMass0;
|
||||
|
||||
Info<< "Added gas mass................. | " << 1e6*addedMass << " mg"
|
||||
<< nl << "Evaporation Continuity Error... | "
|
||||
<< 1e6*(addedMass - evapMass) << " mg" << endl;
|
||||
@ -1,11 +0,0 @@
|
||||
Info<< "Total cylinder mass: " << fvc::domainIntegrate(rho).value() << endl;
|
||||
//Info<< "Total fuel mass: "
|
||||
// << fvc::domainIntegrate(rho*compostion.ft()).value() << endl;
|
||||
|
||||
OFstream logSummaryFile
|
||||
(
|
||||
runTime.path()/("logSummary." + runTime.timeName() + ".dat")
|
||||
);
|
||||
|
||||
logSummaryFile
|
||||
<< "# CA" << " p" << " T" << " u'" << endl;
|
||||
@ -1,3 +0,0 @@
|
||||
dieselFoam.C
|
||||
|
||||
EXE = $(FOAM_APPBIN)/dieselFoam
|
||||
@ -1,38 +0,0 @@
|
||||
EXE_INC = \
|
||||
-I../dieselEngineFoam \
|
||||
-I$(LIB_SRC)/finiteVolume/lnInclude \
|
||||
-I$(LIB_SRC)/turbulenceModels/compressible/turbulenceModel \
|
||||
-I$(LIB_SRC)/lagrangian/basic/lnInclude \
|
||||
-I$(LIB_SRC)/meshTools/lnInclude \
|
||||
-I$(LIB_SRC)/lagrangian/dieselSpray/lnInclude \
|
||||
-I$(LIB_SRC)/thermophysicalModels/properties/liquidProperties/lnInclude \
|
||||
-I$(LIB_SRC)/thermophysicalModels/properties/liquidMixtureProperties/lnInclude \
|
||||
-I$(LIB_SRC)/thermophysicalModels/specie/lnInclude \
|
||||
-I$(LIB_SRC)/thermophysicalModels/thermophysicalFunctions/lnInclude \
|
||||
-I$(LIB_SRC)/thermophysicalModels/reactionThermo/lnInclude \
|
||||
-I$(LIB_SRC)/thermophysicalModels/basic/lnInclude \
|
||||
-I$(LIB_SRC)/thermophysicalModels/laminarFlameSpeed/lnInclude \
|
||||
-I$(LIB_SRC)/../applications/solvers/reactionThermo/XiFoam \
|
||||
-I$(LIB_SRC)/thermophysicalModels/chemistryModel/lnInclude \
|
||||
-I$(LIB_SRC)/ODE/lnInclude \
|
||||
-I$(LIB_SRC)/combustionModels/lnInclude
|
||||
|
||||
EXE_LIBS = \
|
||||
-lcompressibleTurbulenceModel \
|
||||
-lcompressibleRASModels \
|
||||
-lcompressibleLESModels \
|
||||
-lreactionThermophysicalModels \
|
||||
-llagrangian \
|
||||
-lmeshTools \
|
||||
-ldieselSpray \
|
||||
-lliquidProperties \
|
||||
-lliquidMixtureProperties \
|
||||
-lthermophysicalFunctions \
|
||||
-lspecie \
|
||||
-lbasicThermophysicalModels \
|
||||
-llaminarFlameSpeedModels \
|
||||
-lchemistryModel \
|
||||
-lODE \
|
||||
-ldistributionModels \
|
||||
-lfiniteVolume \
|
||||
-lcombustionModels
|
||||
@ -1,118 +0,0 @@
|
||||
/*---------------------------------------------------------------------------*\
|
||||
========= |
|
||||
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
|
||||
\\ / O peration |
|
||||
\\ / A nd | Copyright (C) 2011 OpenFOAM Foundation
|
||||
\\/ M anipulation |
|
||||
-------------------------------------------------------------------------------
|
||||
License
|
||||
This file is part of OpenFOAM.
|
||||
|
||||
OpenFOAM is free software: you can redistribute it and/or modify it
|
||||
under the terms of the GNU General Public License as published by
|
||||
the Free Software Foundation, either version 3 of the License, or
|
||||
(at your option) any later version.
|
||||
|
||||
OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
|
||||
ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
|
||||
FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
|
||||
for more details.
|
||||
|
||||
You should have received a copy of the GNU General Public License
|
||||
along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
|
||||
|
||||
Application
|
||||
dieselFoam
|
||||
|
||||
Description
|
||||
Solver for diesel spray and combustion.
|
||||
|
||||
\*---------------------------------------------------------------------------*/
|
||||
|
||||
#include "fvCFD.H"
|
||||
#include "psiChemistryCombustionModel.H"
|
||||
#include "turbulenceModel.H"
|
||||
#include "psiChemistryModel.H"
|
||||
#include "chemistrySolver.H"
|
||||
#include "spray.H"
|
||||
#include "multivariateScheme.H"
|
||||
#include "IFstream.H"
|
||||
#include "OFstream.H"
|
||||
#include "Switch.H"
|
||||
#include "mathematicalConstants.H"
|
||||
#include "pimpleControl.H"
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
int main(int argc, char *argv[])
|
||||
{
|
||||
#include "setRootCase.H"
|
||||
#include "createTime.H"
|
||||
#include "createMesh.H"
|
||||
#include "createFields.H"
|
||||
#include "readGravitationalAcceleration.H"
|
||||
#include "createSpray.H"
|
||||
#include "initContinuityErrs.H"
|
||||
#include "readTimeControls.H"
|
||||
#include "compressibleCourantNo.H"
|
||||
#include "setInitialDeltaT.H"
|
||||
|
||||
pimpleControl pimple(mesh);
|
||||
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
Info<< "\nStarting time loop\n" << endl;
|
||||
|
||||
while (runTime.run())
|
||||
{
|
||||
#include "compressibleCourantNo.H"
|
||||
#include "setDeltaT.H"
|
||||
|
||||
runTime++;
|
||||
Info<< "Time = " << runTime.timeName() << nl << endl;
|
||||
|
||||
Info<< "Evolving Spray" << endl;
|
||||
|
||||
dieselSpray.evolve();
|
||||
|
||||
Info<< "Solving chemistry" << endl;
|
||||
|
||||
#include "rhoEqn.H"
|
||||
|
||||
// --- Pressure-velocity PIMPLE corrector loop
|
||||
while (pimple.loop())
|
||||
{
|
||||
#include "UEqn.H"
|
||||
#include "YEqn.H"
|
||||
#include "hsEqn.H"
|
||||
|
||||
// --- Pressure corrector loop
|
||||
while (pimple.correct())
|
||||
{
|
||||
#include "pEqn.H"
|
||||
}
|
||||
|
||||
if (pimple.turbCorr())
|
||||
{
|
||||
turbulence->correct();
|
||||
}
|
||||
}
|
||||
|
||||
#include "spraySummary.H"
|
||||
|
||||
rho = thermo.rho();
|
||||
|
||||
runTime.write();
|
||||
|
||||
Info<< "ExecutionTime = " << runTime.elapsedCpuTime() << " s"
|
||||
<< " ClockTime = " << runTime.elapsedClockTime() << " s"
|
||||
<< nl << endl;
|
||||
}
|
||||
|
||||
Info<< "End\n" << endl;
|
||||
|
||||
return 0;
|
||||
}
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -1,72 +0,0 @@
|
||||
rho = thermo.rho();
|
||||
|
||||
volScalarField rAU(1.0/UEqn.A());
|
||||
U = rAU*UEqn.H();
|
||||
|
||||
if (pimple.transonic())
|
||||
{
|
||||
surfaceScalarField phid
|
||||
(
|
||||
"phid",
|
||||
fvc::interpolate(psi)
|
||||
*(
|
||||
(fvc::interpolate(U) & mesh.Sf())
|
||||
+ fvc::ddtPhiCorr(rAU, rho, U, phi)
|
||||
)
|
||||
);
|
||||
|
||||
while (pimple.correctNonOrthogonal())
|
||||
{
|
||||
fvScalarMatrix pEqn
|
||||
(
|
||||
fvm::ddt(psi, p)
|
||||
+ fvm::div(phid, p)
|
||||
- fvm::laplacian(rho*rAU, p)
|
||||
==
|
||||
Sevap
|
||||
);
|
||||
|
||||
pEqn.solve(mesh.solver(p.select(pimple.finalInnerIter())));
|
||||
|
||||
if (pimple.finalNonOrthogonalIter())
|
||||
{
|
||||
phi == pEqn.flux();
|
||||
}
|
||||
}
|
||||
}
|
||||
else
|
||||
{
|
||||
phi =
|
||||
fvc::interpolate(rho)
|
||||
*(
|
||||
(fvc::interpolate(U) & mesh.Sf())
|
||||
+ fvc::ddtPhiCorr(rAU, rho, U, phi)
|
||||
);
|
||||
|
||||
while (pimple.correctNonOrthogonal())
|
||||
{
|
||||
fvScalarMatrix pEqn
|
||||
(
|
||||
fvm::ddt(psi, p)
|
||||
+ fvc::div(phi)
|
||||
- fvm::laplacian(rho*rAU, p)
|
||||
==
|
||||
Sevap
|
||||
);
|
||||
|
||||
pEqn.solve(mesh.solver(p.select(pimple.finalInnerIter())));
|
||||
|
||||
if (pimple.finalNonOrthogonalIter())
|
||||
{
|
||||
phi == pEqn.flux();
|
||||
}
|
||||
}
|
||||
}
|
||||
|
||||
#include "rhoEqn.H"
|
||||
#include "compressibleContinuityErrs.H"
|
||||
|
||||
U -= rAU*fvc::grad(p);
|
||||
U.correctBoundaryConditions();
|
||||
|
||||
DpDt = fvc::DDt(surfaceScalarField("phiU", phi/fvc::interpolate(rho)), p);
|
||||
Reference in New Issue
Block a user