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290584dddc
the in-file lists of authors has been removed in favor of a global list of authors in the LICENSE file. this is done because (a) maintaining a list of authors at the beginning of a file is a major pain in the a**, (b) the list of authors was not accurate in about 85% of all cases where more than one person was involved and (c) this list is not legally binding in any way (the copyright is at the person who authored a given change, if these lists had any legal relevance, one could "aquire" the copyright of the module by forking it and removing the lists...) the only exception of this is the eWoms fork of dune-istl's solvers.hh file. This is beneficial because the authors of that file do not appear in the global list. Further, carrying the fork of that file is required because we would like to use a reasonable convergence criterion for the linear solver. (the solvers from dune-istl do neither support user-defined convergence criteria not do the developers want support for it. (my patch was rejected a few years ago.))
633 lines
22 KiB
C++
633 lines
22 KiB
C++
// -*- mode: C++; tab-width: 4; indent-tabs-mode: nil; c-basic-offset: 4 -*-
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// vi: set et ts=4 sw=4 sts=4:
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/*
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This file is part of the Open Porous Media project (OPM).
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OPM is free software: you can redistribute it and/or modify
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it under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 2 of the License, or
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(at your option) any later version.
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OPM is distributed in the hope that it will be useful,
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but WITHOUT ANY WARRANTY; without even the implied warranty of
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MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the
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GNU General Public License 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 OPM. If not, see <http://www.gnu.org/licenses/>.
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Consult the COPYING file in the top-level source directory of this
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module for the precise wording of the license and the list of
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copyright holders.
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*/
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/*!
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* \file
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*
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* \copydoc Ewoms::CuvetteProblem
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*/
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#ifndef EWOMS_CUVETTE_PROBLEM_HH
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#define EWOMS_CUVETTE_PROBLEM_HH
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#include <opm/material/fluidstates/CompositionalFluidState.hpp>
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#include <opm/material/fluidstates/ImmiscibleFluidState.hpp>
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#include <opm/material/fluidsystems/H2OAirMesityleneFluidSystem.hpp>
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#include <opm/material/fluidmatrixinteractions/ThreePhaseParkerVanGenuchten.hpp>
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#include <opm/material/fluidmatrixinteractions/LinearMaterial.hpp>
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#include <opm/material/heatconduction/Somerton.hpp>
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#include <opm/material/constraintsolvers/MiscibleMultiPhaseComposition.hpp>
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#include <opm/material/fluidmatrixinteractions/MaterialTraits.hpp>
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#include <ewoms/models/pvs/pvsproperties.hh>
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#include <dune/grid/yaspgrid.hh>
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#include <dune/grid/io/file/dgfparser/dgfyasp.hh>
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#include <dune/common/version.hh>
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#include <dune/common/fvector.hh>
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#include <dune/common/fmatrix.hh>
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#include <string>
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namespace Ewoms {
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template <class TypeTag>
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class CuvetteProblem;
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}
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namespace Ewoms {
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namespace Properties {
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// create a new type tag for the cuvette steam injection problem
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NEW_TYPE_TAG(CuvetteBaseProblem);
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// Set the grid type
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SET_TYPE_PROP(CuvetteBaseProblem, Grid, Dune::YaspGrid<2>);
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// Set the problem property
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SET_TYPE_PROP(CuvetteBaseProblem, Problem, Ewoms::CuvetteProblem<TypeTag>);
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// Set the fluid system
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SET_TYPE_PROP(
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CuvetteBaseProblem, FluidSystem,
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Opm::FluidSystems::H2OAirMesitylene<typename GET_PROP_TYPE(TypeTag, Scalar)>);
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// Enable gravity
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SET_BOOL_PROP(CuvetteBaseProblem, EnableGravity, true);
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// Set the maximum time step
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SET_SCALAR_PROP(CuvetteBaseProblem, MaxTimeStepSize, 600.);
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// Set the material Law
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SET_PROP(CuvetteBaseProblem, MaterialLaw)
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{
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private:
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typedef typename GET_PROP_TYPE(TypeTag, Scalar) Scalar;
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typedef typename GET_PROP_TYPE(TypeTag, FluidSystem) FluidSystem;
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typedef Opm::ThreePhaseMaterialTraits<
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Scalar,
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/*wettingPhaseIdx=*/FluidSystem::waterPhaseIdx,
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/*nonWettingPhaseIdx=*/FluidSystem::naplPhaseIdx,
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/*gasPhaseIdx=*/FluidSystem::gasPhaseIdx> Traits;
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public:
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typedef Opm::ThreePhaseParkerVanGenuchten<Traits> type;
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};
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// Set the heat conduction law
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SET_PROP(CuvetteBaseProblem, HeatConductionLaw)
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{
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private:
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typedef typename GET_PROP_TYPE(TypeTag, Scalar) Scalar;
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typedef typename GET_PROP_TYPE(TypeTag, FluidSystem) FluidSystem;
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public:
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// define the material law parameterized by absolute saturations
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typedef Opm::Somerton<FluidSystem, Scalar> type;
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};
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// The default for the end time of the simulation
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SET_SCALAR_PROP(CuvetteBaseProblem, EndTime, 180);
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// The default for the initial time step size of the simulation
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SET_SCALAR_PROP(CuvetteBaseProblem, InitialTimeStepSize, 1);
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// The default DGF file to load
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SET_STRING_PROP(CuvetteBaseProblem, GridFile, "./data/cuvette_11x4.dgf");
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} // namespace Properties
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} // namespace Ewoms
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namespace Ewoms {
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/*!
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* \ingroup TestProblems
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*
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* \brief Non-isothermal three-phase gas injection problem where a hot gas
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* is injected into a unsaturated porous medium with a residually
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* trapped NAPL contamination.
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*
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* The domain is a quasi-two-dimensional container (cuvette). Its
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* dimensions are 1.5 m x 0.74 m. The top and bottom boundaries are
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* closed, the right boundary is a free-flow boundary allowing fluids
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* to escape. From the left, an injection of a hot water-air mixture
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* is injected. The set-up is aimed at remediating an initial NAPL
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* (Non-Aquoeus Phase Liquid) contamination in the domain. The
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* contamination is initially placed partly into the ambient coarse
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* sand and partly into a fine sand lens.
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*
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* This simulation can be varied through assigning different boundary conditions
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* at the left boundary as described in Class (2001):
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* Theorie und numerische Modellierung nichtisothermer Mehrphasenprozesse in
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* NAPL-kontaminierten poroesen Medien, Dissertation, Eigenverlag des Instituts
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* fuer Wasserbau
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*
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* To see the basic effect and the differences to scenarios with pure
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* steam or pure air injection, it is sufficient to simulate this
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* problem to about 2-3 hours simulation time. Complete remediation
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* of the domain requires much longer (about 10 days simulated time).
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*/
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template <class TypeTag>
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class CuvetteProblem : public GET_PROP_TYPE(TypeTag, BaseProblem)
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{
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typedef typename GET_PROP_TYPE(TypeTag, BaseProblem) ParentType;
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typedef typename GET_PROP_TYPE(TypeTag, Scalar) Scalar;
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typedef typename GET_PROP_TYPE(TypeTag, GridView) GridView;
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typedef typename GET_PROP_TYPE(TypeTag, MaterialLaw) MaterialLaw;
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typedef typename GET_PROP_TYPE(TypeTag, MaterialLawParams) MaterialLawParams;
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typedef typename GET_PROP_TYPE(TypeTag, HeatConductionLaw) HeatConductionLaw;
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typedef typename GET_PROP_TYPE(TypeTag, HeatConductionLawParams) HeatConductionLawParams;
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typedef typename GET_PROP_TYPE(TypeTag, EqVector) EqVector;
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typedef typename GET_PROP_TYPE(TypeTag, PrimaryVariables) PrimaryVariables;
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typedef typename GET_PROP_TYPE(TypeTag, RateVector) RateVector;
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typedef typename GET_PROP_TYPE(TypeTag, BoundaryRateVector) BoundaryRateVector;
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typedef typename GET_PROP_TYPE(TypeTag, Simulator) Simulator;
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typedef typename GET_PROP_TYPE(TypeTag, Model) Model;
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typedef typename GET_PROP_TYPE(TypeTag, FluidSystem) FluidSystem;
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// copy some indices for convenience
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typedef typename GET_PROP_TYPE(TypeTag, Indices) Indices;
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enum { numPhases = FluidSystem::numPhases };
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enum { numComponents = FluidSystem::numComponents };
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enum { waterPhaseIdx = FluidSystem::waterPhaseIdx };
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enum { naplPhaseIdx = FluidSystem::naplPhaseIdx };
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enum { gasPhaseIdx = FluidSystem::gasPhaseIdx };
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enum { H2OIdx = FluidSystem::H2OIdx };
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enum { airIdx = FluidSystem::airIdx };
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enum { NAPLIdx = FluidSystem::NAPLIdx };
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enum { conti0EqIdx = Indices::conti0EqIdx };
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// Grid and world dimension
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enum { dimWorld = GridView::dimensionworld };
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typedef typename GridView::ctype CoordScalar;
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typedef Dune::FieldVector<CoordScalar, dimWorld> GlobalPosition;
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typedef Dune::FieldMatrix<Scalar, dimWorld, dimWorld> DimMatrix;
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public:
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/*!
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* \copydoc Doxygen::defaultProblemConstructor
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*/
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CuvetteProblem(Simulator &simulator)
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: ParentType(simulator)
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, eps_(1e-6)
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{ }
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/*!
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* \copydoc FvBaseProblem::finishInit
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*/
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void finishInit()
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{
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ParentType::finishInit();
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if (Valgrind::IsRunning())
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FluidSystem::init(/*minT=*/283.15, /*maxT=*/500.0, /*nT=*/20,
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/*minp=*/0.8e5, /*maxp=*/2e5, /*np=*/10);
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else
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FluidSystem::init(/*minT=*/283.15, /*maxT=*/500.0, /*nT=*/200,
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/*minp=*/0.8e5, /*maxp=*/2e5, /*np=*/100);
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// intrinsic permeabilities
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fineK_ = this->toDimMatrix_(6.28e-12);
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coarseK_ = this->toDimMatrix_(9.14e-10);
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// porosities
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finePorosity_ = 0.42;
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coarsePorosity_ = 0.42;
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// parameters for the capillary pressure law
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#if 1
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// three-phase Parker -- van Genuchten law
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fineMaterialParams_.setVgAlpha(0.0005);
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coarseMaterialParams_.setVgAlpha(0.005);
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fineMaterialParams_.setVgN(4.0);
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coarseMaterialParams_.setVgN(4.0);
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coarseMaterialParams_.setkrRegardsSnr(true);
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fineMaterialParams_.setkrRegardsSnr(true);
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// residual saturations
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fineMaterialParams_.setSwr(0.1201);
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fineMaterialParams_.setSwrx(0.1201);
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fineMaterialParams_.setSnr(0.0701);
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fineMaterialParams_.setSgr(0.0101);
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coarseMaterialParams_.setSwr(0.1201);
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coarseMaterialParams_.setSwrx(0.1201);
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coarseMaterialParams_.setSnr(0.0701);
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coarseMaterialParams_.setSgr(0.0101);
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#else
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// linear material law
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fineMaterialParams_.setPcMinSat(gasPhaseIdx, 0);
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fineMaterialParams_.setPcMaxSat(gasPhaseIdx, 0);
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fineMaterialParams_.setPcMinSat(naplPhaseIdx, 0);
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fineMaterialParams_.setPcMaxSat(naplPhaseIdx, -1000);
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fineMaterialParams_.setPcMinSat(waterPhaseIdx, 0);
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fineMaterialParams_.setPcMaxSat(waterPhaseIdx, -10000);
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coarseMaterialParams_.setPcMinSat(gasPhaseIdx, 0);
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coarseMaterialParams_.setPcMaxSat(gasPhaseIdx, 0);
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coarseMaterialParams_.setPcMinSat(naplPhaseIdx, 0);
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coarseMaterialParams_.setPcMaxSat(naplPhaseIdx, -100);
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coarseMaterialParams_.setPcMinSat(waterPhaseIdx, 0);
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coarseMaterialParams_.setPcMaxSat(waterPhaseIdx, -1000);
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// residual saturations
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fineMaterialParams_.setResidSat(waterPhaseIdx, 0.1201);
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fineMaterialParams_.setResidSat(naplPhaseIdx, 0.0701);
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fineMaterialParams_.setResidSat(gasPhaseIdx, 0.0101);
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coarseMaterialParams_.setResidSat(waterPhaseIdx, 0.1201);
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coarseMaterialParams_.setResidSat(naplPhaseIdx, 0.0701);
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coarseMaterialParams_.setResidSat(gasPhaseIdx, 0.0101);
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#endif
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fineMaterialParams_.finalize();
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coarseMaterialParams_.finalize();
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// initialize parameters for the heat conduction law
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computeHeatCondParams_(heatCondParams_, finePorosity_);
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initInjectFluidState_();
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}
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/*!
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* \name Auxiliary methods
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*/
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//! \{
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/*!
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* \copydoc FvBaseProblem::shouldWriteRestartFile
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*
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* This problem writes a restart file after every time step.
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*/
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bool shouldWriteRestartFile() const
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{ return true; }
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/*!
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* \copydoc FvBaseProblem::name
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*/
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std::string name() const
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{ return std::string("cuvette_") + Model::name(); }
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/*!
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* \copydoc FvBaseProblem::endTimeStep
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*/
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void endTimeStep()
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{
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#ifndef NDEBUG
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this->model().checkConservativeness();
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// Calculate storage terms
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EqVector storage;
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this->model().globalStorage(storage);
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// Write mass balance information for rank 0
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if (this->gridView().comm().rank() == 0) {
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std::cout << "Storage: " << storage << std::endl << std::flush;
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}
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#endif // NDEBUG
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}
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//! \}
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/*!
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* \name Soil parameters
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*/
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//! \{
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/*!
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* \copydoc FvBaseMultiPhaseProblem::temperature
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*/
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template <class Context>
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Scalar temperature(const Context &context, unsigned spaceIdx, unsigned timeIdx) const
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{ return 293.15; /* [K] */ }
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/*!
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* \copydoc FvBaseMultiPhaseProblem::intrinsicPermeability
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*/
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template <class Context>
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const DimMatrix &intrinsicPermeability(const Context &context, unsigned spaceIdx,
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unsigned timeIdx) const
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{
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const GlobalPosition &pos = context.pos(spaceIdx, timeIdx);
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if (isFineMaterial_(pos))
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return fineK_;
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return coarseK_;
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}
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/*!
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* \copydoc FvBaseMultiPhaseProblem::porosity
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*/
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template <class Context>
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Scalar porosity(const Context &context, unsigned spaceIdx, unsigned timeIdx) const
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{
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const GlobalPosition &pos = context.pos(spaceIdx, timeIdx);
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if (isFineMaterial_(pos))
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return finePorosity_;
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else
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return coarsePorosity_;
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}
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/*!
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* \copydoc FvBaseMultiPhaseProblem::materialLawParams
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*/
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template <class Context>
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const MaterialLawParams &materialLawParams(const Context &context,
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unsigned spaceIdx, unsigned timeIdx) const
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{
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const GlobalPosition &pos = context.pos(spaceIdx, timeIdx);
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if (isFineMaterial_(pos))
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return fineMaterialParams_;
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else
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return coarseMaterialParams_;
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}
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/*!
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* \copydoc FvBaseMultiPhaseProblem::heatConductionParams
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*/
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template <class Context>
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const HeatConductionLawParams &
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heatConductionParams(const Context &context, unsigned spaceIdx, unsigned timeIdx) const
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{ return heatCondParams_; }
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/*!
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* \copydoc FvBaseMultiPhaseProblem::heatCapacitySolid
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*/
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template <class Context>
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Scalar heatCapacitySolid(const Context &context, unsigned spaceIdx,
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unsigned timeIdx) const
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{
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return 850 // specific heat capacity [J / (kg K)]
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* 2650; // density of sand [kg/m^3]
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}
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//! \}
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/*!
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* \name Boundary conditions
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*/
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//! \{
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/*!
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* \copydoc FvBaseProblem::boundary
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*/
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template <class Context>
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void boundary(BoundaryRateVector &values, const Context &context,
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unsigned spaceIdx, unsigned timeIdx) const
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{
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const auto &pos = context.pos(spaceIdx, timeIdx);
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if (onRightBoundary_(pos)) {
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Opm::CompositionalFluidState<Scalar, FluidSystem> fs;
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initialFluidState_(fs, context, spaceIdx, timeIdx);
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values.setFreeFlow(context, spaceIdx, timeIdx, fs);
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values.setNoFlow();
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}
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else if (onLeftBoundary_(pos)) {
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// injection
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RateVector molarRate;
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// inject with the same composition as the gas phase of
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// the injection fluid state
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Scalar molarInjectionRate = 0.3435; // [mol/(m^2 s)]
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for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx)
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molarRate[conti0EqIdx + compIdx] =
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-molarInjectionRate
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* injectFluidState_.moleFraction(gasPhaseIdx, compIdx);
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// calculate the total mass injection rate [kg / (m^2 s)
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Scalar massInjectionRate =
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molarInjectionRate
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* injectFluidState_.averageMolarMass(gasPhaseIdx);
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// set the boundary rate vector [J / (m^2 s)]
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values.setMolarRate(molarRate);
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values.setEnthalpyRate(-injectFluidState_.enthalpy(gasPhaseIdx) * massInjectionRate);
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}
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else
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values.setNoFlow();
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}
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//! \}
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/*!
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* \name Volumetric terms
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*/
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//! \{
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/*!
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* \copydoc FvBaseProblem::initial
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*/
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template <class Context>
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void initial(PrimaryVariables &values, const Context &context, unsigned spaceIdx,
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unsigned timeIdx) const
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{
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Opm::CompositionalFluidState<Scalar, FluidSystem> fs;
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initialFluidState_(fs, context, spaceIdx, timeIdx);
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const auto &matParams = materialLawParams(context, spaceIdx, timeIdx);
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values.assignMassConservative(fs, matParams, /*inEquilibrium=*/false);
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}
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/*!
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* \copydoc FvBaseProblem::source
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*
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* For this problem, the source term of all components is 0
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* everywhere.
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*/
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template <class Context>
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void source(RateVector &rate, const Context &context, unsigned spaceIdx,
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unsigned timeIdx) const
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{ rate = Scalar(0.0); }
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//! \}
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private:
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bool onLeftBoundary_(const GlobalPosition &pos) const
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{ return pos[0] < eps_; }
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bool onRightBoundary_(const GlobalPosition &pos) const
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{ return pos[0] > this->boundingBoxMax()[0] - eps_; }
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bool onLowerBoundary_(const GlobalPosition &pos) const
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{ return pos[1] < eps_; }
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bool onUpperBoundary_(const GlobalPosition &pos) const
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{ return pos[1] > this->boundingBoxMax()[1] - eps_; }
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bool isContaminated_(const GlobalPosition &pos) const
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{
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return (0.20 <= pos[0]) && (pos[0] <= 0.80) && (0.4 <= pos[1])
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&& (pos[1] <= 0.65);
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}
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bool isFineMaterial_(const GlobalPosition &pos) const
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{
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if (0.13 <= pos[0] && 1.20 >= pos[0] && 0.32 <= pos[1] && pos[1] <= 0.57)
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return true;
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else if (pos[1] <= 0.15 && 1.20 <= pos[0])
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return true;
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else
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|
return false;
|
|
}
|
|
|
|
template <class FluidState, class Context>
|
|
void initialFluidState_(FluidState &fs, const Context &context,
|
|
unsigned spaceIdx, unsigned timeIdx) const
|
|
{
|
|
const GlobalPosition &pos = context.pos(spaceIdx, timeIdx);
|
|
|
|
fs.setTemperature(293.0 /*[K]*/);
|
|
|
|
Scalar pw = 1e5;
|
|
|
|
if (isContaminated_(pos)) {
|
|
fs.setSaturation(waterPhaseIdx, 0.12);
|
|
fs.setSaturation(naplPhaseIdx, 0.07);
|
|
fs.setSaturation(gasPhaseIdx, 1 - 0.12 - 0.07);
|
|
|
|
// set the capillary pressures
|
|
const auto &matParams = materialLawParams(context, spaceIdx, timeIdx);
|
|
Scalar pc[numPhases];
|
|
MaterialLaw::capillaryPressures(pc, matParams, fs);
|
|
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx)
|
|
fs.setPressure(phaseIdx, pw + (pc[phaseIdx] - pc[waterPhaseIdx]));
|
|
|
|
// compute the phase compositions
|
|
typedef Opm::MiscibleMultiPhaseComposition<Scalar, FluidSystem> MMPC;
|
|
typename FluidSystem::ParameterCache paramCache;
|
|
MMPC::solve(fs, paramCache, /*setViscosity=*/true,
|
|
/*setEnthalpy=*/true);
|
|
}
|
|
else {
|
|
fs.setSaturation(waterPhaseIdx, 0.12);
|
|
fs.setSaturation(gasPhaseIdx, 1 - fs.saturation(waterPhaseIdx));
|
|
fs.setSaturation(naplPhaseIdx, 0);
|
|
|
|
// set the capillary pressures
|
|
const auto &matParams = materialLawParams(context, spaceIdx, timeIdx);
|
|
Scalar pc[numPhases];
|
|
MaterialLaw::capillaryPressures(pc, matParams, fs);
|
|
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx)
|
|
fs.setPressure(phaseIdx, pw + (pc[phaseIdx] - pc[waterPhaseIdx]));
|
|
|
|
// compute the phase compositions
|
|
typedef Opm::MiscibleMultiPhaseComposition<Scalar, FluidSystem> MMPC;
|
|
typename FluidSystem::ParameterCache paramCache;
|
|
MMPC::solve(fs, paramCache, /*setViscosity=*/true,
|
|
/*setEnthalpy=*/true);
|
|
|
|
// set the contaminant mole fractions to zero. this is a
|
|
// little bit hacky...
|
|
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
|
|
fs.setMoleFraction(phaseIdx, NAPLIdx, 0.0);
|
|
|
|
if (phaseIdx == naplPhaseIdx)
|
|
continue;
|
|
|
|
Scalar sumx = 0;
|
|
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx)
|
|
sumx += fs.moleFraction(phaseIdx, compIdx);
|
|
|
|
for (unsigned compIdx = 0; compIdx < numComponents; ++compIdx)
|
|
fs.setMoleFraction(phaseIdx, compIdx,
|
|
fs.moleFraction(phaseIdx, compIdx) / sumx);
|
|
}
|
|
}
|
|
}
|
|
|
|
void computeHeatCondParams_(HeatConductionLawParams ¶ms, Scalar poro)
|
|
{
|
|
Scalar lambdaGranite = 2.8; // [W / (K m)]
|
|
|
|
// create a Fluid state which has all phases present
|
|
Opm::ImmiscibleFluidState<Scalar, FluidSystem> fs;
|
|
fs.setTemperature(293.15);
|
|
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
|
|
fs.setPressure(phaseIdx, 1.0135e5);
|
|
}
|
|
|
|
typename FluidSystem::ParameterCache paramCache;
|
|
paramCache.updateAll(fs);
|
|
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
|
|
Scalar rho = FluidSystem::density(fs, paramCache, phaseIdx);
|
|
fs.setDensity(phaseIdx, rho);
|
|
}
|
|
|
|
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
|
|
Scalar lambdaSaturated;
|
|
if (FluidSystem::isLiquid(phaseIdx)) {
|
|
Scalar lambdaFluid = FluidSystem::thermalConductivity(fs, paramCache, phaseIdx);
|
|
lambdaSaturated =
|
|
std::pow(lambdaGranite, (1 - poro))
|
|
+
|
|
std::pow(lambdaFluid, poro);
|
|
}
|
|
else
|
|
lambdaSaturated = std::pow(lambdaGranite, (1 - poro));
|
|
|
|
params.setFullySaturatedLambda(phaseIdx, lambdaSaturated);
|
|
if (!FluidSystem::isLiquid(phaseIdx))
|
|
params.setVacuumLambda(lambdaSaturated);
|
|
}
|
|
}
|
|
|
|
void initInjectFluidState_()
|
|
{
|
|
injectFluidState_.setTemperature(383.0); // [K]
|
|
injectFluidState_.setPressure(gasPhaseIdx, 1e5); // [Pa]
|
|
injectFluidState_.setSaturation(gasPhaseIdx, 1.0); // [-]
|
|
|
|
Scalar xgH2O = 0.417;
|
|
injectFluidState_.setMoleFraction(gasPhaseIdx, H2OIdx, xgH2O); // [-]
|
|
injectFluidState_.setMoleFraction(gasPhaseIdx, airIdx, 1 - xgH2O); // [-]
|
|
injectFluidState_.setMoleFraction(gasPhaseIdx, NAPLIdx, 0.0); // [-]
|
|
|
|
// set the specific enthalpy of the gas phase
|
|
typename FluidSystem::ParameterCache paramCache;
|
|
paramCache.updatePhase(injectFluidState_, gasPhaseIdx);
|
|
|
|
Scalar h = FluidSystem::enthalpy(injectFluidState_, paramCache, gasPhaseIdx);
|
|
injectFluidState_.setEnthalpy(gasPhaseIdx, h);
|
|
}
|
|
|
|
DimMatrix fineK_;
|
|
DimMatrix coarseK_;
|
|
|
|
Scalar finePorosity_;
|
|
Scalar coarsePorosity_;
|
|
|
|
MaterialLawParams fineMaterialParams_;
|
|
MaterialLawParams coarseMaterialParams_;
|
|
|
|
HeatConductionLawParams heatCondParams_;
|
|
|
|
Opm::CompositionalFluidState<Scalar, FluidSystem> injectFluidState_;
|
|
|
|
const Scalar eps_;
|
|
};
|
|
} // namespace Ewoms
|
|
|
|
#endif
|