The interface for fvModels has been modified to improve its application
to "proxy" equations. That is, equations that are not straightforward
statements of conservation laws in OpenFOAM's usual convention.
A standard conservation law typically takes the following form:
fvMatrix<scalar> psiEqn
(
fvm::ddt(alpha, rho, psi)
+ <fluxes>
==
<sources>
);
A proxy equation, on the other hand, may be a derivation or
rearrangement of a law like this, and may be linearised in terms of a
different variable.
The pressure equation is the most common example of a proxy equation. It
represents a statement of the conservation of volume or mass, but it is
a rearrangement of the original continuity equation, and it has been
linearised in terms of a different variable; the pressure. Another
example is that in the pre-predictor of a VoF solver the
phase-continuity equation is constructed, but it is linearised in terms
of volume fraction rather than density.
In these situations, fvModels sources are now applied by calling:
fvModels().sourceProxy(<conserved-fields ...>, <equation-field>)
Where <conserved-fields ...> are (alpha, rho, psi), (rho, psi), just
(psi), or are omitted entirely (for volume continuity), and the
<equation-field> is the field associated with the proxy equation. This
produces a source term identical in value to the following call:
fvModels().source(<conserved-fields ...>)
It is only the linearisation in terms of <equation-field> that differs
between these two calls.
This change permits much greater flexibility in the handling of mass and
volume sources than the previous name-based system did. All the relevant
fields are available, dimensions can be used in the logic to determine
what sources are being constructed, and sources relating to a given
conservation law all share the same function.
This commit adds the functionality for injection-type sources in the
compressibleVoF solver. A following commit will add a volume source
model for use in incompressible solvers.
237 lines
6.9 KiB
C++
237 lines
6.9 KiB
C++
/*---------------------------------------------------------------------------*\
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========= |
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
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\\ / O peration | Website: https://openfoam.org
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\\ / A nd | Copyright (C) 2023 OpenFOAM Foundation
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\\/ M anipulation |
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-------------------------------------------------------------------------------
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License
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This file is part of OpenFOAM.
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OpenFOAM is free software: you can redistribute it and/or modify it
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under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 3 of the License, or
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(at your option) any later version.
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OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
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ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
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FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
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for more details.
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You should have received a copy of the GNU General Public License
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along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
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Class
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Foam::solvers::incompressibleDriftFlux
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Description
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Solver module for 2 incompressible fluids using the mixture approach with
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the drift-flux approximation for relative motion of the phases, with
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optional mesh motion and mesh topology changes including adaptive
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re-meshing.
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The momentum and other fluid properties are of the "mixture" and a single
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momentum equation is solved with mixture transport modelling in which a
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single laminar, RAS or LES model is selected to model the momentum stress.
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Uses the flexible PIMPLE (PISO-SIMPLE) solution for time-resolved and
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pseudo-transient and steady simulations.
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Optional fvModels and fvConstraints are provided to enhance the simulation
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in many ways including adding various sources, Lagrangian
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particles, surface film etc. and constraining or limiting the solution.
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SourceFiles
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incompressibleDriftFlux.C
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See also
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Foam::solvers::VoFSolver
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Foam::solvers::twoPhaseSolver
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Foam::solvers::compressibleVoF
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\*---------------------------------------------------------------------------*/
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#ifndef incompressibleDriftFlux_H
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#define incompressibleDriftFlux_H
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#include "twoPhaseSolver.H"
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#include "incompressibleDriftFluxMixture.H"
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#include "relativeVelocityModel.H"
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#include "momentumTransportModel.H"
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#include "compressibleMomentumTransportModels.H"
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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namespace Foam
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{
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namespace solvers
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{
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/*---------------------------------------------------------------------------*\
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Class incompressibleDriftFlux Declaration
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\*---------------------------------------------------------------------------*/
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class incompressibleDriftFlux
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:
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public twoPhaseSolver
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{
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protected:
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// Phase properties
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//- The compressible two-phase mixture
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incompressibleDriftFluxMixture& mixture;
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// Thermophysical properties
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//- Static pressure field
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volScalarField p;
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// Pressure reference
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//- Pressure reference
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Foam::pressureReference pressureReference_;
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// Momentum transport
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//- Pointer to the dispersed phase relative velocity model
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autoPtr<relativeVelocityModel> relativeVelocity;
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//- Pointer to the momentum transport model
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autoPtr<compressible::momentumTransportModel> momentumTransport;
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private:
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// Private Member Functions
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//- Correct the cached Courant numbers
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virtual void correctCoNum();
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protected:
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// Protected Member Functions
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//- Return the pressure reference
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virtual const Foam::pressureReference& pressureReference() const
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{
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return pressureReference_;
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}
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//- The flow is incompressible
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virtual bool incompressible() const
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{
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return true;
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}
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//- Is the flow divergent?
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// i.e. includes phase-fraction sources
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virtual bool divergent() const
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{
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return
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fvModels().addsSupToField(alpha1.name())
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|| fvModels().addsSupToField(alpha2.name());
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}
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//- Return the mixture compressibility/density
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// Not required for incompressible fluids
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virtual tmp<volScalarField> psiByRho() const
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{
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return tmp<volScalarField>(nullptr);
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}
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virtual tmp<surfaceScalarField> alphaPhi
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(
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const surfaceScalarField& phi,
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const volScalarField& alpha,
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const dictionary& alphaControls
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);
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//- Adjust the rDeltaT in the vicinity of the interface
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virtual void setInterfaceRDeltaT(volScalarField& rDeltaT);
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//- Calculate the alpha equation sources
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virtual void alphaSuSp
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(
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tmp<volScalarField::Internal>& Su,
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tmp<volScalarField::Internal>& Sp
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);
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//- Correct the interface properties following mesh-change
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// and phase-fraction update
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virtual void correctInterface();
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//- Return the interface surface tension force for the momentum equation
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virtual tmp<surfaceScalarField> surfaceTensionForce() const;
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//- Return the momentum equation stress term
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virtual tmp<fvVectorMatrix> divDevTau(volVectorField& U)
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{
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return
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relativeVelocity->divDevTau()
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+ momentumTransport->divDevTau(U);
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}
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public:
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//- Runtime type information
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TypeName("incompressibleDriftFlux");
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// Constructors
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//- Construct from region mesh
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incompressibleDriftFlux(fvMesh& mesh);
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//- Disallow default bitwise copy construction
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incompressibleDriftFlux(const incompressibleDriftFlux&) = delete;
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//- Destructor
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virtual ~incompressibleDriftFlux();
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// Member Functions
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//- Return the current maximum time-step for stable solution
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virtual scalar maxDeltaT() const;
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//- Called at the start of the PIMPLE loop
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virtual void prePredictor();
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//- Construct and solve the energy equation,
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// convert to temperature
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// and update thermophysical and transport properties
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virtual void thermophysicalPredictor();
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//- Construct and solve the pressure equation in the PISO loop
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virtual void pressureCorrector();
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//- Correct the momentum and thermophysical transport modelling
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virtual void postCorrector();
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// Member Operators
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//- Disallow default bitwise assignment
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void operator=(const incompressibleDriftFlux&) = delete;
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};
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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} // End namespace solvers
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} // End namespace Foam
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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#endif
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// ************************************************************************* //
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