mu and k access methods and explicit viscous stress term in UEqn
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0dfbd072ed
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41cb4714c3
4 changed files with 73 additions and 42 deletions
6
UEqn.H
6
UEqn.H
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@ -2,11 +2,15 @@
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MRF.correctBoundaryVelocity(U);
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tmp<fvVectorMatrix> tUEqn
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(
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fvm::ddt(rho, U) + fvm::div(phi, U)
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+ MRF.DDt(rho, U)
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+ turbulence->divDevRhoReff(U)
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+ (
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- fvc::div(diff.mu()*Foam::dev2(Foam::T(fvc::grad(U))))
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- fvm::laplacian(diff.mu(), U)
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)
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==
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fvOptions(rho, U)
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);
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@ -287,6 +287,32 @@ Foam::diffusivityModel::diffusivityModel(const psiReactionThermo& thermo)
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:
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thermo_(thermo),
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D_(thermo_.composition().species().size()),
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mu_
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(
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IOobject
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(
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"mu",
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thermo_.composition().Y(0).mesh().time().timeName(),
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thermo_.composition().Y(0).mesh(),
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IOobject::NO_READ,
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IOobject::AUTO_WRITE
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),
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thermo_.composition().Y(0).mesh(),
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dimensionedScalar("zero", dimPressure*dimTime, 0.0)
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),
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k_
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(
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IOobject
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(
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"lambda",
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thermo_.composition().Y(0).mesh().time().timeName(),
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thermo_.composition().Y(0).mesh(),
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IOobject::NO_READ,
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IOobject::AUTO_WRITE
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),
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thermo_.composition().Y(0).mesh(),
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dimensionedScalar("zero", dimArea/dimTime, 0.0)
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),
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neutrals_(thermo_.composition().species().size()),
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ions_(thermo_.composition().species().size()),
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ecs_(thermo_.composition().species().size()),
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@ -481,40 +507,6 @@ Foam::diffusivityModel::diffusivityModel(const psiReactionThermo& thermo)
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}
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}
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mu_.set
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(
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new volScalarField
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(
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IOobject
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(
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"mu",
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mesh.time().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("zero", dimArea/dimTime, 0.0)
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)
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);
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k_.set
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(
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new volScalarField
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(
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IOobject
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(
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"lambda",
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mesh.time().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("zero", dimArea/dimTime, 0.0)
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)
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);
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forAll(species_, i)
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{
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D_.set
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@ -540,7 +532,9 @@ Foam::diffusivityModel::diffusivityModel(const psiReactionThermo& thermo)
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Foam::diffusivityModel::diffusivityModel(const diffusivityModel& dm)
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:
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thermo_(dm.thermo_)
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thermo_(dm.thermo_),
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mu_(dm.mu_),
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k_(dm.k_)
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{}
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@ -678,8 +672,8 @@ void Foam::diffusivityModel::correct()
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D_[i][celli] = Di[i];
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}
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mu_()[celli] = mixAvgMu(muI, localX, Wpure);
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k_()[celli] = mixAvgK(kI, localX) / rhoi / Cpi;
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mu_[celli] = mixAvgMu(muI, localX, Wpure);
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k_[celli] = mixAvgK(kI, localX) / rhoi / Cpi;
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}
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@ -755,8 +749,8 @@ void Foam::diffusivityModel::correct()
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D_[i].boundaryFieldRef()[patchi][facei] = Di[i];
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}
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mu_().boundaryFieldRef()[patchi][facei] = mixAvgMu(muI, localX, Wpure);
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k_().boundaryFieldRef()[patchi][facei] = mixAvgK(kI, localX) / rhoi / Cpi;
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mu_.boundaryFieldRef()[patchi][facei] = mixAvgMu(muI, localX, Wpure);
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k_.boundaryFieldRef()[patchi][facei] = mixAvgK(kI, localX) / rhoi / Cpi;
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}
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}
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@ -73,10 +73,10 @@ class diffusivityModel
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PtrList<volScalarField> D_;
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//- Mixture averaged viscosity field
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autoPtr<volScalarField> mu_;
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volScalarField mu_;
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//- Mixture averaged thermal conductivity field
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autoPtr<volScalarField> k_;
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volScalarField k_;
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//- Electron object
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autoPtr<Electron> electron_;
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@ -174,6 +174,15 @@ public:
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// Access
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inline volScalarField& mu();
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inline const volScalarField& mu() const;
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inline volScalarField& k();
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inline const volScalarField& k() const;
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// Check
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// Edit
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@ -37,6 +37,30 @@ License
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// * * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * //
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Foam::volScalarField& Foam::diffusivityModel::mu()
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{
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return mu_;
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}
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const Foam::volScalarField& Foam::diffusivityModel::mu() const
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{
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return mu_;
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}
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Foam::volScalarField& Foam::diffusivityModel::k()
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{
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return k_;
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}
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const Foam::volScalarField& Foam::diffusivityModel::k() const
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{
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return k_;
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}
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// * * * * * * * * * * * * * * * Member Operators * * * * * * * * * * * * * //
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