mirror of
https://github.com/OPM/opm-simulators.git
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1579 lines
69 KiB
C++
1579 lines
69 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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* \brief Contains the classes required to extend the black-oil model by solvents.
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*/
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#ifndef EWOMS_BLACK_OIL_SOLVENT_MODULE_HH
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#define EWOMS_BLACK_OIL_SOLVENT_MODULE_HH
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#include "blackoilproperties.hh"
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#include <opm/common/Exceptions.hpp>
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#include <opm/models/blackoil/blackoilsolventparams.hh>
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#include <opm/models/io/vtkblackoilsolventmodule.hh>
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#include <opm/models/common/quantitycallbacks.hh>
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#include <opm/material/fluidsystems/blackoilpvt/SolventPvt.hpp>
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#if HAVE_ECL_INPUT
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#include <opm/input/eclipse/EclipseState/EclipseState.hpp>
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#include <opm/input/eclipse/EclipseState/Tables/SsfnTable.hpp>
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#include <opm/input/eclipse/EclipseState/Tables/Sof2Table.hpp>
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#include <opm/input/eclipse/EclipseState/Tables/MsfnTable.hpp>
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#include <opm/input/eclipse/EclipseState/Tables/PmiscTable.hpp>
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#include <opm/input/eclipse/EclipseState/Tables/MiscTable.hpp>
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#include <opm/input/eclipse/EclipseState/Tables/SorwmisTable.hpp>
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#include <opm/input/eclipse/EclipseState/Tables/SgcwmisTable.hpp>
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#include <opm/input/eclipse/EclipseState/Tables/TlpmixpaTable.hpp>
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#endif
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#include <opm/material/common/Valgrind.hpp>
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#include <dune/common/fvector.hh>
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#include <string>
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namespace Opm {
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/*!
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* \ingroup BlackOil
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* \brief Contains the high level supplements required to extend the black oil
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* model by solvents.
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*/
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template <class TypeTag, bool enableSolventV = getPropValue<TypeTag, Properties::EnableSolvent>()>
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class BlackOilSolventModule
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{
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using Scalar = GetPropType<TypeTag, Properties::Scalar>;
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using Evaluation = GetPropType<TypeTag, Properties::Evaluation>;
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using PrimaryVariables = GetPropType<TypeTag, Properties::PrimaryVariables>;
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using IntensiveQuantities = GetPropType<TypeTag, Properties::IntensiveQuantities>;
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using ExtensiveQuantities = GetPropType<TypeTag, Properties::ExtensiveQuantities>;
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using ElementContext = GetPropType<TypeTag, Properties::ElementContext>;
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using FluidSystem = GetPropType<TypeTag, Properties::FluidSystem>;
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using Model = GetPropType<TypeTag, Properties::Model>;
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using Simulator = GetPropType<TypeTag, Properties::Simulator>;
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using EqVector = GetPropType<TypeTag, Properties::EqVector>;
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using RateVector = GetPropType<TypeTag, Properties::RateVector>;
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using Indices = GetPropType<TypeTag, Properties::Indices>;
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using Toolbox = MathToolbox<Evaluation>;
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using SolventPvt = typename BlackOilSolventParams<Scalar>::SolventPvt;
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using Co2GasPvt = typename BlackOilSolventParams<Scalar>::Co2GasPvt;
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using H2GasPvt = typename BlackOilSolventParams<Scalar>::H2GasPvt;
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using BrineCo2Pvt = typename BlackOilSolventParams<Scalar>::BrineCo2Pvt;
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using BrineH2Pvt = typename BlackOilSolventParams<Scalar>::BrineH2Pvt;
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using TabulatedFunction = typename BlackOilSolventParams<Scalar>::TabulatedFunction;
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static constexpr unsigned solventSaturationIdx = Indices::solventSaturationIdx;
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static constexpr unsigned contiSolventEqIdx = Indices::contiSolventEqIdx;
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static constexpr unsigned enableSolvent = enableSolventV;
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static constexpr unsigned numEq = getPropValue<TypeTag, Properties::NumEq>();
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static constexpr unsigned numPhases = FluidSystem::numPhases;
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static constexpr bool blackoilConserveSurfaceVolume = getPropValue<TypeTag, Properties::BlackoilConserveSurfaceVolume>();
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static constexpr int waterPhaseIdx = FluidSystem::waterPhaseIdx;
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public:
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#if HAVE_ECL_INPUT
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/*!
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* \brief Initialize all internal data structures needed by the solvent module
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*/
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static void initFromState(const EclipseState& eclState, const Schedule& schedule)
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{
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// some sanity checks: if solvents are enabled, the SOLVENT keyword must be
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// present, if solvents are disabled the keyword must not be present.
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if (enableSolvent && !eclState.runspec().phases().active(Phase::SOLVENT))
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throw std::runtime_error("Non-trivial solvent treatment requested at compile "
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"time, but the deck does not contain the SOLVENT keyword");
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else if (!enableSolvent && eclState.runspec().phases().active(Phase::SOLVENT))
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throw std::runtime_error("Solvent treatment disabled at compile time, but the deck "
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"contains the SOLVENT keyword");
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if (!eclState.runspec().phases().active(Phase::SOLVENT))
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return; // solvent treatment is supposed to be disabled
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params_.co2sol_ = eclState.runspec().co2Sol();
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params_.h2sol_ = eclState.runspec().h2Sol();
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if (isCO2Sol() && isH2Sol()) {
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throw std::runtime_error("CO2SOL and H2SOL can not be used together");
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}
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if (isCO2Sol() || isH2Sol() ) {
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if (isCO2Sol()) {
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params_.co2GasPvt_.initFromState(eclState, schedule);
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params_.brineCo2Pvt_.initFromState(eclState, schedule);
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} else {
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params_.h2GasPvt_.initFromState(eclState, schedule);
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params_.brineH2Pvt_.initFromState(eclState, schedule);
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}
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if (eclState.getSimulationConfig().hasDISGASW()) {
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params_.rsSolw_active_ = true;
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}
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} else
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params_.solventPvt_.initFromState(eclState, schedule);
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const auto& tableManager = eclState.getTableManager();
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// initialize the objects which deal with the SSFN keyword
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const auto& ssfnTables = tableManager.getSsfnTables();
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unsigned numSatRegions = tableManager.getTabdims().getNumSatTables();
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params_.setNumSatRegions(numSatRegions);
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for (unsigned satRegionIdx = 0; satRegionIdx < numSatRegions; ++ satRegionIdx) {
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const auto& ssfnTable = ssfnTables.template getTable<SsfnTable>(satRegionIdx);
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params_.ssfnKrg_[satRegionIdx].setXYContainers(ssfnTable.getSolventFractionColumn(),
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ssfnTable.getGasRelPermMultiplierColumn(),
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/*sortInput=*/true);
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params_.ssfnKrs_[satRegionIdx].setXYContainers(ssfnTable.getSolventFractionColumn(),
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ssfnTable.getSolventRelPermMultiplierColumn(),
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/*sortInput=*/true);
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}
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// initialize the objects needed for miscible solvent and oil simulations
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params_.isMiscible_ = false;
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if (!eclState.getTableManager().getMiscTables().empty()) {
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params_.isMiscible_ = true;
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unsigned numMiscRegions = 1;
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// misicible hydrocabon relative permeability wrt water
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const auto& sof2Tables = tableManager.getSof2Tables();
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if (!sof2Tables.empty()) {
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// resize the attributes of the object
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params_.sof2Krn_.resize(numSatRegions);
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for (unsigned satRegionIdx = 0; satRegionIdx < numSatRegions; ++ satRegionIdx) {
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const auto& sof2Table = sof2Tables.template getTable<Sof2Table>(satRegionIdx);
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params_.sof2Krn_[satRegionIdx].setXYContainers(sof2Table.getSoColumn(),
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sof2Table.getKroColumn(),
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/*sortInput=*/true);
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}
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}
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else if(eclState.runspec().phases().active(Phase::OIL))
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throw std::runtime_error("SOF2 must be specified in MISCIBLE (SOLVENT and OIL) runs\n");
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const auto& miscTables = tableManager.getMiscTables();
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if (!miscTables.empty()) {
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assert(numMiscRegions == miscTables.size());
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// resize the attributes of the object
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params_.misc_.resize(numMiscRegions);
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for (unsigned miscRegionIdx = 0; miscRegionIdx < numMiscRegions; ++miscRegionIdx) {
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const auto& miscTable = miscTables.template getTable<MiscTable>(miscRegionIdx);
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// solventFraction = Ss / (Ss + Sg);
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const auto& solventFraction = miscTable.getSolventFractionColumn();
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const auto& misc = miscTable.getMiscibilityColumn();
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params_.misc_[miscRegionIdx].setXYContainers(solventFraction, misc);
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}
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}
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else
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throw std::runtime_error("MISC must be specified in MISCIBLE (SOLVENT) runs\n");
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// resize the attributes of the object
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params_.pmisc_.resize(numMiscRegions);
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const auto& pmiscTables = tableManager.getPmiscTables();
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if (!pmiscTables.empty()) {
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assert(numMiscRegions == pmiscTables.size());
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx) {
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const auto& pmiscTable = pmiscTables.template getTable<PmiscTable>(regionIdx);
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// Copy data
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const auto& po = pmiscTable.getOilPhasePressureColumn();
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const auto& pmisc = pmiscTable.getMiscibilityColumn();
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params_.pmisc_[regionIdx].setXYContainers(po, pmisc);
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}
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}
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else {
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std::vector<double> x = {0.0,1.0e20};
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std::vector<double> y = {1.0,1.0};
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TabulatedFunction constant = TabulatedFunction(2, x, y);
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx) {
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params_.pmisc_[regionIdx] = constant;
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}
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}
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// miscible relative permeability multipleiers
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params_.msfnKrsg_.resize(numSatRegions);
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params_.msfnKro_.resize(numSatRegions);
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const auto& msfnTables = tableManager.getMsfnTables();
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if (!msfnTables.empty()) {
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assert(numSatRegions == msfnTables.size());
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for (unsigned regionIdx = 0; regionIdx < numSatRegions; ++regionIdx) {
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const MsfnTable& msfnTable = msfnTables.template getTable<MsfnTable>(regionIdx);
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// Copy data
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// Ssg = Ss + Sg;
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const auto& Ssg = msfnTable.getGasPhaseFractionColumn();
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const auto& krsg = msfnTable.getGasSolventRelpermMultiplierColumn();
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const auto& kro = msfnTable.getOilRelpermMultiplierColumn();
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params_.msfnKrsg_[regionIdx].setXYContainers(Ssg, krsg);
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params_.msfnKro_[regionIdx].setXYContainers(Ssg, kro);
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}
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}
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else {
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std::vector<double> x = {0.0,1.0};
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std::vector<double> y = {1.0,0.0};
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TabulatedFunction unit = TabulatedFunction(2, x, x);
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TabulatedFunction invUnit = TabulatedFunction(2, x, y);
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for (unsigned regionIdx = 0; regionIdx < numSatRegions; ++regionIdx) {
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params_.setMsfn(regionIdx, unit, invUnit);
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}
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}
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// resize the attributes of the object
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params_.sorwmis_.resize(numMiscRegions);
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const auto& sorwmisTables = tableManager.getSorwmisTables();
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if (!sorwmisTables.empty()) {
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assert(numMiscRegions == sorwmisTables.size());
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx) {
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const auto& sorwmisTable = sorwmisTables.template getTable<SorwmisTable>(regionIdx);
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// Copy data
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const auto& sw = sorwmisTable.getWaterSaturationColumn();
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const auto& sorwmis = sorwmisTable.getMiscibleResidualOilColumn();
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params_.sorwmis_[regionIdx].setXYContainers(sw, sorwmis);
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}
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}
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else {
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// default
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std::vector<double> x = {0.0,1.0};
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std::vector<double> y = {0.0,0.0};
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TabulatedFunction zero = TabulatedFunction(2, x, y);
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx) {
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params_.sorwmis_[regionIdx] = zero;
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}
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}
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// resize the attributes of the object
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params_.sgcwmis_.resize(numMiscRegions);
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const auto& sgcwmisTables = tableManager.getSgcwmisTables();
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if (!sgcwmisTables.empty()) {
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assert(numMiscRegions == sgcwmisTables.size());
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx) {
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const auto& sgcwmisTable = sgcwmisTables.template getTable<SgcwmisTable>(regionIdx);
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// Copy data
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const auto& sw = sgcwmisTable.getWaterSaturationColumn();
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const auto& sgcwmis = sgcwmisTable.getMiscibleResidualGasColumn();
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params_.sgcwmis_[regionIdx].setXYContainers(sw, sgcwmis);
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}
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}
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else {
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// default
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std::vector<double> x = {0.0,1.0};
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std::vector<double> y = {0.0,0.0};
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TabulatedFunction zero = TabulatedFunction(2, x, y);
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx)
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params_.sgcwmis_[regionIdx] = zero;
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}
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const auto& tlmixpar = eclState.getTableManager().getTLMixpar();
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if (!tlmixpar.empty()) {
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// resize the attributes of the object
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params_.tlMixParamViscosity_.resize(numMiscRegions);
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params_.tlMixParamDensity_.resize(numMiscRegions);
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assert(numMiscRegions == tlmixpar.size());
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx) {
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const auto& tlp = tlmixpar[regionIdx];
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params_.tlMixParamViscosity_[regionIdx] = tlp.viscosity_parameter;
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params_.tlMixParamDensity_[regionIdx] = tlp.density_parameter;
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}
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}
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else
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throw std::runtime_error("TLMIXPAR must be specified in MISCIBLE (SOLVENT) runs\n");
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// resize the attributes of the object
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params_.tlPMixTable_.resize(numMiscRegions);
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if (!eclState.getTableManager().getTlpmixpaTables().empty()) {
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const auto& tlpmixparTables = tableManager.getTlpmixpaTables();
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if (!tlpmixparTables.empty()) {
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assert(numMiscRegions == tlpmixparTables.size());
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx) {
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const auto& tlpmixparTable = tlpmixparTables.template getTable<TlpmixpaTable>(regionIdx);
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// Copy data
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const auto& po = tlpmixparTable.getOilPhasePressureColumn();
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const auto& tlpmixpa = tlpmixparTable.getMiscibilityColumn();
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params_.tlPMixTable_[regionIdx].setXYContainers(po, tlpmixpa);
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}
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}
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else {
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// if empty keyword. Try to use the pmisc table as default.
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if (params_.pmisc_.size() > 0)
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params_.tlPMixTable_ = params_.pmisc_;
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else
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throw std::invalid_argument("If the pressure dependent TL values in "
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"TLPMIXPA is defaulted (no entries), then "
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"the PMISC tables must be specified.");
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}
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}
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else {
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// default
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std::vector<double> x = {0.0,1.0e20};
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std::vector<double> y = {1.0,1.0};
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TabulatedFunction ones = TabulatedFunction(2, x, y);
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for (unsigned regionIdx = 0; regionIdx < numMiscRegions; ++regionIdx)
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params_.tlPMixTable_[regionIdx] = ones;
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}
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}
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}
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#endif
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/*!
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* \brief Specify the solvent PVT of a all PVT regions.
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*/
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static void setSolventPvt(const SolventPvt& value)
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{ params_.solventPvt_ = value; }
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static void setIsMiscible(const bool isMiscible)
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{ params_.isMiscible_ = isMiscible; }
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/*!
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* \brief Register all run-time parameters for the black-oil solvent module.
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*/
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static void registerParameters()
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{
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if constexpr (enableSolvent)
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VtkBlackOilSolventModule<TypeTag>::registerParameters();
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}
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/*!
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* \brief Register all solvent specific VTK and ECL output modules.
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*/
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static void registerOutputModules(Model& model,
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Simulator& simulator)
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{
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if constexpr (enableSolvent)
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model.addOutputModule(new VtkBlackOilSolventModule<TypeTag>(simulator));
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}
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static bool primaryVarApplies(unsigned pvIdx)
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{
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if constexpr (enableSolvent)
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return pvIdx == solventSaturationIdx;
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else
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return false;
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}
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static std::string primaryVarName([[maybe_unused]] unsigned pvIdx)
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{
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assert(primaryVarApplies(pvIdx));
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return "saturation_solvent";
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}
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static Scalar primaryVarWeight([[maybe_unused]] unsigned pvIdx)
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{
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assert(primaryVarApplies(pvIdx));
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// TODO: it may be beneficial to chose this differently.
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return static_cast<Scalar>(1.0);
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}
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static bool eqApplies(unsigned eqIdx)
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{
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if constexpr (enableSolvent)
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return eqIdx == contiSolventEqIdx;
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else
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return false;
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}
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static std::string eqName([[maybe_unused]] unsigned eqIdx)
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{
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assert(eqApplies(eqIdx));
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return "conti^solvent";
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}
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static Scalar eqWeight([[maybe_unused]] unsigned eqIdx)
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{
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assert(eqApplies(eqIdx));
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// TODO: it may be beneficial to chose this differently.
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return static_cast<Scalar>(1.0);
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}
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template <class LhsEval>
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static void addStorage(Dune::FieldVector<LhsEval, numEq>& storage,
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const IntensiveQuantities& intQuants)
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{
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if constexpr (enableSolvent) {
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if constexpr (blackoilConserveSurfaceVolume) {
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storage[contiSolventEqIdx] +=
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Toolbox::template decay<LhsEval>(intQuants.porosity())
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* Toolbox::template decay<LhsEval>(intQuants.solventSaturation())
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* Toolbox::template decay<LhsEval>(intQuants.solventInverseFormationVolumeFactor());
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if (isSolubleInWater()) {
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storage[contiSolventEqIdx] += Toolbox::template decay<LhsEval>(intQuants.porosity())
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* Toolbox::template decay<LhsEval>(intQuants.fluidState().saturation(waterPhaseIdx))
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* Toolbox::template decay<LhsEval>(intQuants.fluidState().invB(waterPhaseIdx))
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* Toolbox::template decay<LhsEval>(intQuants.rsSolw());
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}
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}
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else {
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storage[contiSolventEqIdx] +=
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Toolbox::template decay<LhsEval>(intQuants.porosity())
|
|
* Toolbox::template decay<LhsEval>(intQuants.solventSaturation())
|
|
* Toolbox::template decay<LhsEval>(intQuants.solventDensity());
|
|
if (isSolubleInWater()) {
|
|
storage[contiSolventEqIdx] += Toolbox::template decay<LhsEval>(intQuants.porosity())
|
|
* Toolbox::template decay<LhsEval>(intQuants.fluidState().saturation(waterPhaseIdx))
|
|
* Toolbox::template decay<LhsEval>(intQuants.fluidState().density(waterPhaseIdx))
|
|
* Toolbox::template decay<LhsEval>(intQuants.rsSolw());
|
|
}
|
|
|
|
}
|
|
}
|
|
}
|
|
|
|
static void computeFlux([[maybe_unused]] RateVector& flux,
|
|
[[maybe_unused]] const ElementContext& elemCtx,
|
|
[[maybe_unused]] unsigned scvfIdx,
|
|
[[maybe_unused]] unsigned timeIdx)
|
|
|
|
{
|
|
if constexpr (enableSolvent) {
|
|
const auto& extQuants = elemCtx.extensiveQuantities(scvfIdx, timeIdx);
|
|
|
|
unsigned upIdx = extQuants.solventUpstreamIndex();
|
|
unsigned inIdx = extQuants.interiorIndex();
|
|
const auto& up = elemCtx.intensiveQuantities(upIdx, timeIdx);
|
|
|
|
if constexpr (blackoilConserveSurfaceVolume) {
|
|
if (upIdx == inIdx)
|
|
flux[contiSolventEqIdx] =
|
|
extQuants.solventVolumeFlux()
|
|
*up.solventInverseFormationVolumeFactor();
|
|
else
|
|
flux[contiSolventEqIdx] =
|
|
extQuants.solventVolumeFlux()
|
|
*decay<Scalar>(up.solventInverseFormationVolumeFactor());
|
|
|
|
|
|
if (isSolubleInWater()) {
|
|
if (upIdx == inIdx)
|
|
flux[contiSolventEqIdx] =
|
|
extQuants.volumeFlux(waterPhaseIdx)
|
|
* up.fluidState().invB(waterPhaseIdx)
|
|
* up.rsSolw();
|
|
else
|
|
flux[contiSolventEqIdx] =
|
|
extQuants.volumeFlux(waterPhaseIdx)
|
|
*decay<Scalar>(up.fluidState().invB(waterPhaseIdx))
|
|
*decay<Scalar>(up.rsSolw());
|
|
}
|
|
}
|
|
else {
|
|
if (upIdx == inIdx)
|
|
flux[contiSolventEqIdx] =
|
|
extQuants.solventVolumeFlux()
|
|
*up.solventDensity();
|
|
else
|
|
flux[contiSolventEqIdx] =
|
|
extQuants.solventVolumeFlux()
|
|
*decay<Scalar>(up.solventDensity());
|
|
|
|
|
|
if (isSolubleInWater()) {
|
|
if (upIdx == inIdx)
|
|
flux[contiSolventEqIdx] =
|
|
extQuants.volumeFlux(waterPhaseIdx)
|
|
* up.fluidState().density(waterPhaseIdx)
|
|
* up.rsSolw();
|
|
else
|
|
flux[contiSolventEqIdx] =
|
|
extQuants.volumeFlux(waterPhaseIdx)
|
|
*decay<Scalar>(up.fluidState().density(waterPhaseIdx))
|
|
*decay<Scalar>(up.rsSolw());
|
|
}
|
|
}
|
|
}
|
|
}
|
|
|
|
/*!
|
|
* \brief Assign the solvent specific primary variables to a PrimaryVariables object
|
|
*/
|
|
static void assignPrimaryVars(PrimaryVariables& priVars,
|
|
Scalar solventSaturation,
|
|
Scalar solventRsw)
|
|
{
|
|
if constexpr (!enableSolvent) {
|
|
priVars.setPrimaryVarsMeaningSolvent(PrimaryVariables::SolventMeaning::Disabled);
|
|
return;
|
|
}
|
|
// Determine the meaning of the solvent primary variables
|
|
if (solventSaturation > 0 || !isSolubleInWater()) {
|
|
priVars.setPrimaryVarsMeaningSolvent(PrimaryVariables::SolventMeaning::Ss);
|
|
priVars[solventSaturationIdx] = solventSaturation;
|
|
} else {
|
|
priVars.setPrimaryVarsMeaningSolvent(PrimaryVariables::SolventMeaning::Rsolw);
|
|
priVars[solventSaturationIdx] = solventRsw;
|
|
}
|
|
}
|
|
|
|
/*!
|
|
* \brief Do a Newton-Raphson update the primary variables of the solvents.
|
|
*/
|
|
static void updatePrimaryVars(PrimaryVariables& newPv,
|
|
const PrimaryVariables& oldPv,
|
|
const EqVector& delta)
|
|
{
|
|
if constexpr (enableSolvent)
|
|
// do a plain unchopped Newton update
|
|
newPv[solventSaturationIdx] = oldPv[solventSaturationIdx] - delta[solventSaturationIdx];
|
|
}
|
|
|
|
/*!
|
|
* \brief Return how much a Newton-Raphson update is considered an error
|
|
*/
|
|
static Scalar computeUpdateError(const PrimaryVariables&,
|
|
const EqVector&)
|
|
{
|
|
// do not consider consider the cange of solvent primary variables for
|
|
// convergence
|
|
// TODO: maybe this should be changed
|
|
return static_cast<Scalar>(0.0);
|
|
}
|
|
|
|
/*!
|
|
* \brief Return how much a residual is considered an error
|
|
*/
|
|
static Scalar computeResidualError(const EqVector& resid)
|
|
{
|
|
// do not weight the residual of solvents when it comes to convergence
|
|
return std::abs(Toolbox::scalarValue(resid[contiSolventEqIdx]));
|
|
}
|
|
|
|
template <class DofEntity>
|
|
static void serializeEntity(const Model& model, std::ostream& outstream, const DofEntity& dof)
|
|
{
|
|
if constexpr (enableSolvent) {
|
|
unsigned dofIdx = model.dofMapper().index(dof);
|
|
|
|
const PrimaryVariables& priVars = model.solution(/*timeIdx=*/0)[dofIdx];
|
|
outstream << priVars[solventSaturationIdx];
|
|
}
|
|
}
|
|
|
|
template <class DofEntity>
|
|
static void deserializeEntity(Model& model, std::istream& instream, const DofEntity& dof)
|
|
{
|
|
if constexpr (enableSolvent) {
|
|
unsigned dofIdx = model.dofMapper().index(dof);
|
|
|
|
PrimaryVariables& priVars0 = model.solution(/*timeIdx=*/0)[dofIdx];
|
|
PrimaryVariables& priVars1 = model.solution(/*timeIdx=*/1)[dofIdx];
|
|
|
|
instream >> priVars0[solventSaturationIdx];
|
|
|
|
// set the primary variables for the beginning of the current time step.
|
|
priVars1 = priVars0[solventSaturationIdx];
|
|
}
|
|
}
|
|
|
|
static const SolventPvt& solventPvt()
|
|
{
|
|
return params_.solventPvt_;
|
|
}
|
|
|
|
|
|
static const Co2GasPvt& co2GasPvt()
|
|
{
|
|
return params_.co2GasPvt_;
|
|
}
|
|
|
|
static const H2GasPvt& h2GasPvt()
|
|
{
|
|
return params_.h2GasPvt_;
|
|
}
|
|
|
|
static const BrineCo2Pvt& brineCo2Pvt()
|
|
{
|
|
return params_.brineCo2Pvt_;
|
|
}
|
|
|
|
static const BrineH2Pvt& brineH2Pvt()
|
|
{
|
|
return params_.brineH2Pvt_;
|
|
}
|
|
|
|
static const TabulatedFunction& ssfnKrg(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned satnumRegionIdx = elemCtx.problem().satnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.ssfnKrg_[satnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& ssfnKrs(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned satnumRegionIdx = elemCtx.problem().satnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.ssfnKrs_[satnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& sof2Krn(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned satnumRegionIdx = elemCtx.problem().satnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.sof2Krn_[satnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& misc(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned miscnumRegionIdx = elemCtx.problem().miscnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.misc_[miscnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& pmisc(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned miscnumRegionIdx = elemCtx.problem().miscnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.pmisc_[miscnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& msfnKrsg(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned satnumRegionIdx = elemCtx.problem().satnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.msfnKrsg_[satnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& msfnKro(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned satnumRegionIdx = elemCtx.problem().satnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.msfnKro_[satnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& sorwmis(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned miscnumRegionIdx = elemCtx.problem().miscnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.sorwmis_[miscnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& sgcwmis(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned miscnumRegionIdx = elemCtx.problem().miscnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.sgcwmis_[miscnumRegionIdx];
|
|
}
|
|
|
|
static const TabulatedFunction& tlPMixTable(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned miscnumRegionIdx = elemCtx.problem().miscnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.tlPMixTable_[miscnumRegionIdx];
|
|
}
|
|
|
|
static const Scalar& tlMixParamViscosity(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned miscnumRegionIdx = elemCtx.problem().miscnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.tlMixParamViscosity_[miscnumRegionIdx];
|
|
}
|
|
|
|
static const Scalar& tlMixParamDensity(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
unsigned miscnumRegionIdx = elemCtx.problem().miscnumRegionIndex(elemCtx, scvIdx, timeIdx);
|
|
return params_.tlMixParamDensity_[miscnumRegionIdx];
|
|
}
|
|
|
|
static bool isMiscible()
|
|
{
|
|
return params_.isMiscible_;
|
|
}
|
|
|
|
template <class Value>
|
|
static const Value solubilityLimit(unsigned pvtIdx, const Value& temperature, const Value& pressure, const Value& saltConcentration)
|
|
{
|
|
if (!isSolubleInWater())
|
|
return 0.0;
|
|
|
|
assert(isCO2Sol() || isH2Sol());
|
|
if (isCO2Sol())
|
|
return brineCo2Pvt().saturatedGasDissolutionFactor(pvtIdx, temperature, pressure, saltConcentration);
|
|
else
|
|
return brineH2Pvt().saturatedGasDissolutionFactor(pvtIdx, temperature, pressure, saltConcentration);
|
|
}
|
|
|
|
static bool isSolubleInWater()
|
|
{
|
|
return params_.rsSolw_active_;
|
|
}
|
|
|
|
static bool isCO2Sol()
|
|
{
|
|
return params_.co2sol_;
|
|
}
|
|
|
|
static bool isH2Sol()
|
|
{
|
|
return params_.h2sol_;
|
|
}
|
|
|
|
private:
|
|
static BlackOilSolventParams<Scalar> params_; // the krg(Fs) column of the SSFN table
|
|
};
|
|
|
|
template <class TypeTag, bool enableSolventV>
|
|
BlackOilSolventParams<typename BlackOilSolventModule<TypeTag, enableSolventV>::Scalar>
|
|
BlackOilSolventModule<TypeTag, enableSolventV>::params_;
|
|
|
|
/*!
|
|
* \ingroup BlackOil
|
|
* \class Opm::BlackOilSolventIntensiveQuantities
|
|
*
|
|
* \brief Provides the volumetric quantities required for the equations needed by the
|
|
* solvents extension of the black-oil model.
|
|
*/
|
|
template <class TypeTag, bool enableSolventV = getPropValue<TypeTag, Properties::EnableSolvent>()>
|
|
class BlackOilSolventIntensiveQuantities
|
|
{
|
|
using Implementation = GetPropType<TypeTag, Properties::IntensiveQuantities>;
|
|
|
|
using Scalar = GetPropType<TypeTag, Properties::Scalar>;
|
|
using Evaluation = GetPropType<TypeTag, Properties::Evaluation>;
|
|
using PrimaryVariables = GetPropType<TypeTag, Properties::PrimaryVariables>;
|
|
using FluidSystem = GetPropType<TypeTag, Properties::FluidSystem>;
|
|
using MaterialLaw = GetPropType<TypeTag, Properties::MaterialLaw>;
|
|
using Indices = GetPropType<TypeTag, Properties::Indices>;
|
|
using ElementContext = GetPropType<TypeTag, Properties::ElementContext>;
|
|
|
|
using SolventModule = BlackOilSolventModule<TypeTag>;
|
|
|
|
enum { numPhases = getPropValue<TypeTag, Properties::NumPhases>() };
|
|
static constexpr int solventSaturationIdx = Indices::solventSaturationIdx;
|
|
static constexpr int oilPhaseIdx = FluidSystem::oilPhaseIdx;
|
|
static constexpr int gasPhaseIdx = FluidSystem::gasPhaseIdx;
|
|
static constexpr int waterPhaseIdx = FluidSystem::waterPhaseIdx;
|
|
static constexpr double cutOff = 1e-12;
|
|
|
|
|
|
public:
|
|
/*!
|
|
* \brief Called before the saturation functions are doing their magic
|
|
*
|
|
* At this point, the saturations of the fluid state correspond to those if the phases
|
|
* were pure hydrocarbons.
|
|
*/
|
|
void solventPreSatFuncUpdate_(const ElementContext& elemCtx,
|
|
unsigned dofIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
const PrimaryVariables& priVars = elemCtx.primaryVars(dofIdx, timeIdx);
|
|
|
|
auto& fs = asImp_().fluidState_;
|
|
solventSaturation_ = 0.0;
|
|
if (priVars.primaryVarsMeaningSolvent() == PrimaryVariables::SolventMeaning::Ss) {
|
|
solventSaturation_ = priVars.makeEvaluation(solventSaturationIdx, timeIdx, elemCtx.linearizationType());
|
|
}
|
|
|
|
hydrocarbonSaturation_ = fs.saturation(gasPhaseIdx);
|
|
|
|
// apply a cut-off. Don't waste calculations if no solvent
|
|
if (solventSaturation().value() < cutOff)
|
|
return;
|
|
|
|
// make the saturation of the gas phase which is used by the saturation functions
|
|
// the sum of the solvent "saturation" and the saturation the hydrocarbon gas.
|
|
fs.setSaturation(gasPhaseIdx, hydrocarbonSaturation_ + solventSaturation_);
|
|
}
|
|
|
|
/*!
|
|
* \brief Called after the saturation functions have been doing their magic
|
|
*
|
|
* After this function, all saturations, pressures
|
|
* and relative permeabilities must be final. (i.e., the "hydrocarbon
|
|
* saturations".)
|
|
*/
|
|
void solventPostSatFuncUpdate_(const ElementContext& elemCtx,
|
|
unsigned dofIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
// revert the gas "saturation" of the fluid state back to the saturation of the
|
|
// hydrocarbon gas.
|
|
auto& fs = asImp_().fluidState_;
|
|
fs.setSaturation(gasPhaseIdx, hydrocarbonSaturation_);
|
|
|
|
|
|
// update rsSolw. This needs to be done after the pressure is defined in the fluid state.
|
|
rsSolw_ = 0.0;
|
|
const PrimaryVariables& priVars = elemCtx.primaryVars(dofIdx, timeIdx);
|
|
if (priVars.primaryVarsMeaningSolvent() == PrimaryVariables::SolventMeaning::Ss) {
|
|
rsSolw_ = SolventModule::solubilityLimit(asImp_().pvtRegionIndex(), fs.temperature(waterPhaseIdx), fs.pressure(waterPhaseIdx), fs.saltConcentration());
|
|
} else if (priVars.primaryVarsMeaningSolvent() == PrimaryVariables::SolventMeaning::Rsolw) {
|
|
rsSolw_ = priVars.makeEvaluation(solventSaturationIdx, timeIdx, elemCtx.linearizationType());
|
|
}
|
|
|
|
solventMobility_ = 0.0;
|
|
|
|
// apply a cut-off. Don't waste calculations if no solvent
|
|
if (solventSaturation().value() < cutOff)
|
|
return;
|
|
|
|
// Pressure effects on capillary pressure miscibility
|
|
if (SolventModule::isMiscible()) {
|
|
const Evaluation& p = FluidSystem::phaseIsActive(oilPhaseIdx)? fs.pressure(oilPhaseIdx) : fs.pressure(gasPhaseIdx);
|
|
const Evaluation pmisc = SolventModule::pmisc(elemCtx, dofIdx, timeIdx).eval(p, /*extrapolate=*/true);
|
|
const Evaluation& pgImisc = fs.pressure(gasPhaseIdx);
|
|
|
|
// compute capillary pressure for miscible fluid
|
|
const auto& problem = elemCtx.problem();
|
|
Evaluation pgMisc = 0.0;
|
|
std::array<Evaluation, numPhases> pC;
|
|
const auto& materialParams = problem.materialLawParams(elemCtx, dofIdx, timeIdx);
|
|
MaterialLaw::capillaryPressures(pC, materialParams, fs);
|
|
|
|
//oil is the reference phase for pressure
|
|
const auto linearizationType = elemCtx.linearizationType();
|
|
if (priVars.primaryVarsMeaningPressure() == PrimaryVariables::PressureMeaning::Pg)
|
|
pgMisc = priVars.makeEvaluation(Indices::pressureSwitchIdx, timeIdx, linearizationType);
|
|
else {
|
|
const Evaluation& po = priVars.makeEvaluation(Indices::pressureSwitchIdx, timeIdx, linearizationType);
|
|
pgMisc = po + (pC[gasPhaseIdx] - pC[oilPhaseIdx]);
|
|
}
|
|
|
|
fs.setPressure(gasPhaseIdx, pmisc * pgMisc + (1.0 - pmisc) * pgImisc);
|
|
}
|
|
|
|
|
|
Evaluation gasSolventSat = hydrocarbonSaturation_ + solventSaturation_;
|
|
|
|
if (gasSolventSat.value() < cutOff) // avoid division by zero
|
|
return;
|
|
|
|
Evaluation Fhydgas = hydrocarbonSaturation_/gasSolventSat;
|
|
Evaluation Fsolgas = solventSaturation_/gasSolventSat;
|
|
|
|
// account for miscibility of oil and solvent
|
|
if (SolventModule::isMiscible() && FluidSystem::phaseIsActive(oilPhaseIdx)) {
|
|
const auto& misc = SolventModule::misc(elemCtx, dofIdx, timeIdx);
|
|
const auto& pmisc = SolventModule::pmisc(elemCtx, dofIdx, timeIdx);
|
|
const Evaluation& p = FluidSystem::phaseIsActive(oilPhaseIdx)? fs.pressure(oilPhaseIdx) : fs.pressure(gasPhaseIdx);
|
|
const Evaluation miscibility = misc.eval(Fsolgas, /*extrapolate=*/true) * pmisc.eval(p, /*extrapolate=*/true);
|
|
|
|
// TODO adjust endpoints of sn and ssg
|
|
unsigned cellIdx = elemCtx.globalSpaceIndex(dofIdx, timeIdx);
|
|
const auto& materialLawManager = elemCtx.problem().materialLawManager();
|
|
const auto& scaledDrainageInfo =
|
|
materialLawManager->oilWaterScaledEpsInfoDrainage(cellIdx);
|
|
|
|
const Scalar& sogcr = scaledDrainageInfo.Sogcr;
|
|
Evaluation sor = sogcr;
|
|
if (FluidSystem::phaseIsActive(waterPhaseIdx)) {
|
|
const Evaluation& sw = fs.saturation(waterPhaseIdx);
|
|
const auto& sorwmis = SolventModule::sorwmis(elemCtx, dofIdx, timeIdx);
|
|
sor = miscibility * sorwmis.eval(sw, /*extrapolate=*/true) + (1.0 - miscibility) * sogcr;
|
|
}
|
|
const Scalar& sgcr = scaledDrainageInfo.Sgcr;
|
|
Evaluation sgc = sgcr;
|
|
if (FluidSystem::phaseIsActive(waterPhaseIdx)) {
|
|
const Evaluation& sw = fs.saturation(waterPhaseIdx);
|
|
const auto& sgcwmis = SolventModule::sgcwmis(elemCtx, dofIdx, timeIdx);
|
|
sgc = miscibility * sgcwmis.eval(sw, /*extrapolate=*/true) + (1.0 - miscibility) * sgcr;
|
|
}
|
|
|
|
Evaluation oilGasSolventSat = gasSolventSat;
|
|
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
|
|
oilGasSolventSat += fs.saturation(oilPhaseIdx);
|
|
}
|
|
const Evaluation zero = 0.0;
|
|
const Evaluation oilGasSolventEffSat = std::max(oilGasSolventSat - sor - sgc, zero);
|
|
|
|
Evaluation F_totalGas = 0.0;
|
|
if (oilGasSolventEffSat.value() > cutOff) {
|
|
const Evaluation gasSolventEffSat = std::max(gasSolventSat - sgc, zero);
|
|
F_totalGas = gasSolventEffSat / oilGasSolventEffSat;
|
|
}
|
|
const auto& msfnKro = SolventModule::msfnKro(elemCtx, dofIdx, timeIdx);
|
|
const auto& msfnKrsg = SolventModule::msfnKrsg(elemCtx, dofIdx, timeIdx);
|
|
const auto& sof2Krn = SolventModule::sof2Krn(elemCtx, dofIdx, timeIdx);
|
|
|
|
const Evaluation mkrgt = msfnKrsg.eval(F_totalGas, /*extrapolate=*/true) * sof2Krn.eval(oilGasSolventSat, /*extrapolate=*/true);
|
|
const Evaluation mkro = msfnKro.eval(F_totalGas, /*extrapolate=*/true) * sof2Krn.eval(oilGasSolventSat, /*extrapolate=*/true);
|
|
|
|
Evaluation& kro = asImp_().mobility_[oilPhaseIdx];
|
|
Evaluation& krg = asImp_().mobility_[gasPhaseIdx];
|
|
|
|
// combine immiscible and miscible part of the relperm
|
|
krg *= (1.0 - miscibility);
|
|
krg += miscibility * mkrgt;
|
|
kro *= (1.0 - miscibility);
|
|
kro += miscibility * mkro;
|
|
}
|
|
|
|
// compute the mobility of the solvent "phase" and modify the gas phase
|
|
const auto& ssfnKrg = SolventModule::ssfnKrg(elemCtx, dofIdx, timeIdx);
|
|
const auto& ssfnKrs = SolventModule::ssfnKrs(elemCtx, dofIdx, timeIdx);
|
|
|
|
Evaluation& krg = asImp_().mobility_[gasPhaseIdx];
|
|
solventMobility_ = krg * ssfnKrs.eval(Fsolgas, /*extrapolate=*/true);
|
|
krg *= ssfnKrg.eval(Fhydgas, /*extrapolate=*/true);
|
|
|
|
}
|
|
|
|
/*!
|
|
* \brief Update the intensive PVT properties needed to handle solvents from the
|
|
* primary variables.
|
|
*
|
|
* At this point the pressures and saturations of the fluid state are correct.
|
|
*/
|
|
void solventPvtUpdate_(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
const auto& iq = asImp_();
|
|
unsigned pvtRegionIdx = iq.pvtRegionIndex();
|
|
const Evaluation& T = iq.fluidState().temperature(gasPhaseIdx);
|
|
const Evaluation& p = iq.fluidState().pressure(gasPhaseIdx);
|
|
|
|
const Evaluation rv = 0.0;
|
|
const Evaluation rvw = 0.0;
|
|
if (SolventModule::isCO2Sol() || SolventModule::isH2Sol() ){
|
|
if (SolventModule::isCO2Sol()) {
|
|
const auto& co2gasPvt = SolventModule::co2GasPvt();
|
|
solventInvFormationVolumeFactor_ = co2gasPvt.inverseFormationVolumeFactor(pvtRegionIdx, T, p, rv, rvw);
|
|
solventRefDensity_ = co2gasPvt.gasReferenceDensity(pvtRegionIdx);
|
|
solventViscosity_ = co2gasPvt.viscosity(pvtRegionIdx, T, p, rv, rvw);
|
|
|
|
const auto& brineCo2Pvt = SolventModule::brineCo2Pvt();
|
|
auto& fs = asImp_().fluidState_;
|
|
const auto& bw = brineCo2Pvt.inverseFormationVolumeFactor(pvtRegionIdx, T, p, rsSolw());
|
|
|
|
const auto denw = bw*brineCo2Pvt.waterReferenceDensity(pvtRegionIdx)
|
|
+ rsSolw()*bw*brineCo2Pvt.gasReferenceDensity(pvtRegionIdx);
|
|
fs.setDensity(waterPhaseIdx, denw);
|
|
fs.setInvB(waterPhaseIdx, bw);
|
|
Evaluation& mobw = asImp_().mobility_[waterPhaseIdx];
|
|
const auto& muWat = fs.viscosity(waterPhaseIdx);
|
|
const auto& muWatEff = brineCo2Pvt.viscosity(pvtRegionIdx, T, p, rsSolw());
|
|
mobw *= muWat / muWatEff;
|
|
} else {
|
|
const auto& h2gasPvt = SolventModule::h2GasPvt();
|
|
solventInvFormationVolumeFactor_ = h2gasPvt.inverseFormationVolumeFactor(pvtRegionIdx, T, p, rv, rvw);
|
|
solventRefDensity_ = h2gasPvt.gasReferenceDensity(pvtRegionIdx);
|
|
solventViscosity_ = h2gasPvt.viscosity(pvtRegionIdx, T, p, rv, rvw);
|
|
|
|
const auto& brineH2Pvt = SolventModule::brineH2Pvt();
|
|
auto& fs = asImp_().fluidState_;
|
|
const auto& bw = brineH2Pvt.inverseFormationVolumeFactor(pvtRegionIdx, T, p, rsSolw());
|
|
|
|
const auto denw = bw*brineH2Pvt.waterReferenceDensity(pvtRegionIdx)
|
|
+ rsSolw()*bw*brineH2Pvt.gasReferenceDensity(pvtRegionIdx);
|
|
fs.setDensity(waterPhaseIdx, denw);
|
|
fs.setInvB(waterPhaseIdx, bw);
|
|
Evaluation& mobw = asImp_().mobility_[waterPhaseIdx];
|
|
const auto& muWat = fs.viscosity(waterPhaseIdx);
|
|
const auto& muWatEff = brineH2Pvt.viscosity(pvtRegionIdx, T, p, rsSolw());
|
|
mobw *= muWat / muWatEff;
|
|
}
|
|
} else {
|
|
const auto& solventPvt = SolventModule::solventPvt();
|
|
solventInvFormationVolumeFactor_ = solventPvt.inverseFormationVolumeFactor(pvtRegionIdx, T, p);
|
|
solventRefDensity_ = solventPvt.referenceDensity(pvtRegionIdx);
|
|
solventViscosity_ = solventPvt.viscosity(pvtRegionIdx, T, p);
|
|
}
|
|
|
|
solventDensity_ = solventInvFormationVolumeFactor_*solventRefDensity_;
|
|
effectiveProperties(elemCtx, scvIdx, timeIdx);
|
|
|
|
solventMobility_ /= solventViscosity_;
|
|
|
|
|
|
}
|
|
|
|
const Evaluation& solventSaturation() const
|
|
{ return solventSaturation_; }
|
|
|
|
const Evaluation& rsSolw() const
|
|
{ return rsSolw_; }
|
|
|
|
const Evaluation& solventDensity() const
|
|
{ return solventDensity_; }
|
|
|
|
const Evaluation& solventViscosity() const
|
|
{ return solventViscosity_; }
|
|
|
|
const Evaluation& solventMobility() const
|
|
{ return solventMobility_; }
|
|
|
|
const Evaluation& solventInverseFormationVolumeFactor() const
|
|
{ return solventInvFormationVolumeFactor_; }
|
|
|
|
// This could be stored pr pvtRegion instead
|
|
const Scalar& solventRefDensity() const
|
|
{ return solventRefDensity_; }
|
|
|
|
private:
|
|
// Computes the effective properties based on
|
|
// Todd-Longstaff mixing model.
|
|
void effectiveProperties(const ElementContext& elemCtx,
|
|
unsigned scvIdx,
|
|
unsigned timeIdx)
|
|
{
|
|
if (!SolventModule::isMiscible())
|
|
return;
|
|
|
|
// Don't waste calculations if no solvent
|
|
// Apply a cut-off for small and negative solvent saturations
|
|
if (solventSaturation() < cutOff)
|
|
return;
|
|
|
|
// We plan to update the fluidstate with the effective
|
|
// properties
|
|
auto& fs = asImp_().fluidState_;
|
|
|
|
// Compute effective saturations
|
|
Evaluation oilEffSat = 0.0;
|
|
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
|
|
oilEffSat = fs.saturation(oilPhaseIdx);
|
|
}
|
|
Evaluation gasEffSat = fs.saturation(gasPhaseIdx);
|
|
Evaluation solventEffSat = solventSaturation();
|
|
if (FluidSystem::phaseIsActive(waterPhaseIdx)) {
|
|
const auto& sorwmis = SolventModule::sorwmis(elemCtx, scvIdx, timeIdx);
|
|
const auto& sgcwmis = SolventModule::sgcwmis(elemCtx, scvIdx, timeIdx);
|
|
const Evaluation zero = 0.0;
|
|
const Evaluation& sw = fs.saturation(waterPhaseIdx);
|
|
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
|
|
oilEffSat = std::max(oilEffSat - sorwmis.eval(sw, /*extrapolate=*/true), zero);
|
|
}
|
|
gasEffSat = std::max(gasEffSat - sgcwmis.eval(sw, /*extrapolate=*/true), zero);
|
|
solventEffSat = std::max(solventEffSat - sgcwmis.eval(sw, /*extrapolate=*/true), zero);
|
|
}
|
|
const Evaluation oilGasSolventEffSat = oilEffSat + gasEffSat + solventEffSat;
|
|
const Evaluation oilSolventEffSat = oilEffSat + solventEffSat;
|
|
const Evaluation solventGasEffSat = solventEffSat + gasEffSat;
|
|
|
|
// Compute effective viscosities
|
|
|
|
// Mixing parameter for viscosity
|
|
// The pressureMixingParameter represent the miscibility of the solvent while the mixingParameterViscosity the effect of the porous media.
|
|
// The pressureMixingParameter is not implemented in ecl100.
|
|
const Evaluation& p = FluidSystem::phaseIsActive(oilPhaseIdx)? fs.pressure(oilPhaseIdx) : fs.pressure(gasPhaseIdx);
|
|
// account for pressure effects
|
|
const auto& pmiscTable = SolventModule::pmisc(elemCtx, scvIdx, timeIdx);
|
|
const Evaluation pmisc = pmiscTable.eval(p, /*extrapolate=*/true);
|
|
const auto& tlPMixTable = SolventModule::tlPMixTable(elemCtx, scvIdx, timeIdx);
|
|
const Evaluation tlMixParamMu = SolventModule::tlMixParamViscosity(elemCtx, scvIdx, timeIdx) * tlPMixTable.eval(p, /*extrapolate=*/true);
|
|
|
|
const Evaluation& muGas = fs.viscosity(gasPhaseIdx);
|
|
const Evaluation& muSolvent = solventViscosity_;
|
|
|
|
assert(muGas.value() > 0);
|
|
assert(muSolvent.value() > 0);
|
|
const Evaluation muGasPow = pow(muGas, 0.25);
|
|
const Evaluation muSolventPow = pow(muSolvent, 0.25);
|
|
|
|
Evaluation muMixSolventGas = muGas;
|
|
if (solventGasEffSat > cutOff)
|
|
muMixSolventGas *= muSolvent / pow(((gasEffSat / solventGasEffSat) * muSolventPow) + ((solventEffSat / solventGasEffSat) * muGasPow) , 4.0);
|
|
|
|
Evaluation muOil = 1.0;
|
|
Evaluation muOilPow = 1.0;
|
|
Evaluation muMixOilSolvent = 1.0;
|
|
Evaluation muOilEff = 1.0;
|
|
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
|
|
muOil = fs.viscosity(oilPhaseIdx);
|
|
assert(muOil.value() > 0);
|
|
muOilPow = pow(muOil, 0.25);
|
|
muMixOilSolvent = muOil;
|
|
if (oilSolventEffSat > cutOff)
|
|
muMixOilSolvent *= muSolvent / pow(((oilEffSat / oilSolventEffSat) * muSolventPow) + ((solventEffSat / oilSolventEffSat) * muOilPow) , 4.0);
|
|
|
|
muOilEff = pow(muOil,1.0 - tlMixParamMu) * pow(muMixOilSolvent, tlMixParamMu);
|
|
}
|
|
Evaluation muMixSolventGasOil = muOil;
|
|
if (oilGasSolventEffSat > cutOff)
|
|
muMixSolventGasOil *= muSolvent * muGas / pow(((oilEffSat / oilGasSolventEffSat) * muSolventPow * muGasPow)
|
|
+ ((solventEffSat / oilGasSolventEffSat) * muOilPow * muGasPow) + ((gasEffSat / oilGasSolventEffSat) * muSolventPow * muOilPow), 4.0);
|
|
|
|
Evaluation muGasEff = pow(muGas,1.0 - tlMixParamMu) * pow(muMixSolventGas, tlMixParamMu);
|
|
Evaluation muSolventEff = pow(muSolvent,1.0 - tlMixParamMu) * pow(muMixSolventGasOil, tlMixParamMu);
|
|
|
|
// Compute effective densities
|
|
const Evaluation& rhoGas = fs.density(gasPhaseIdx);
|
|
Evaluation rhoOil = 0.0;
|
|
if (FluidSystem::phaseIsActive(oilPhaseIdx))
|
|
rhoOil = fs.density(oilPhaseIdx);
|
|
|
|
const Evaluation& rhoSolvent = solventDensity_;
|
|
|
|
// Mixing parameter for density
|
|
// The pressureMixingParameter represent the miscibility of the solvent while the mixingParameterDenisty the effect of the porous media.
|
|
// The pressureMixingParameter is not implemented in ecl100.
|
|
const Evaluation tlMixParamRho = SolventModule::tlMixParamDensity(elemCtx, scvIdx, timeIdx) * tlPMixTable.eval(p, /*extrapolate=*/true);
|
|
|
|
// compute effective viscosities for density calculations. These have to
|
|
// be recomputed as a different mixing parameter may be used.
|
|
const Evaluation muOilEffPow = pow(pow(muOil, 1.0 - tlMixParamRho) * pow(muMixOilSolvent, tlMixParamRho), 0.25);
|
|
const Evaluation muGasEffPow = pow(pow(muGas, 1.0 - tlMixParamRho) * pow(muMixSolventGas, tlMixParamRho), 0.25);
|
|
const Evaluation muSolventEffPow = pow(pow(muSolvent, 1.0 - tlMixParamRho) * pow(muMixSolventGasOil, tlMixParamRho), 0.25);
|
|
|
|
const Evaluation oilGasEffSaturation = oilEffSat + gasEffSat;
|
|
Evaluation sof = 0.0;
|
|
Evaluation sgf = 0.0;
|
|
if (oilGasEffSaturation.value() > cutOff) {
|
|
sof = oilEffSat / oilGasEffSaturation;
|
|
sgf = gasEffSat / oilGasEffSaturation;
|
|
}
|
|
|
|
const Evaluation muSolventOilGasPow = muSolventPow * ((sgf * muOilPow) + (sof * muGasPow));
|
|
|
|
Evaluation rhoMixSolventGasOil = 0.0;
|
|
if (oilGasSolventEffSat.value() > cutOff)
|
|
rhoMixSolventGasOil = (rhoOil * oilEffSat / oilGasSolventEffSat) + (rhoGas * gasEffSat / oilGasSolventEffSat) + (rhoSolvent * solventEffSat / oilGasSolventEffSat);
|
|
|
|
Evaluation rhoGasEff = 0.0;
|
|
if (std::abs(muSolventPow.value() - muGasPow.value()) < cutOff)
|
|
rhoGasEff = ((1.0 - tlMixParamRho) * rhoGas) + (tlMixParamRho * rhoMixSolventGasOil);
|
|
else {
|
|
const Evaluation solventGasEffFraction = (muGasPow * (muSolventPow - muGasEffPow)) / (muGasEffPow * (muSolventPow - muGasPow));
|
|
rhoGasEff = (rhoGas * solventGasEffFraction) + (rhoSolvent * (1.0 - solventGasEffFraction));
|
|
}
|
|
|
|
Evaluation rhoSolventEff = 0.0;
|
|
if (std::abs((muSolventOilGasPow.value() - (muOilPow.value() * muGasPow.value()))) < cutOff)
|
|
rhoSolventEff = ((1.0 - tlMixParamRho) * rhoSolvent) + (tlMixParamRho * rhoMixSolventGasOil);
|
|
else {
|
|
const Evaluation sfraction_se = (muSolventOilGasPow - (muOilPow * muGasPow * muSolventPow / muSolventEffPow)) / (muSolventOilGasPow - (muOilPow * muGasPow));
|
|
rhoSolventEff = (rhoSolvent * sfraction_se) + (rhoGas * sgf * (1.0 - sfraction_se)) + (rhoOil * sof * (1.0 - sfraction_se));
|
|
}
|
|
|
|
// compute invB from densities.
|
|
unsigned pvtRegionIdx = asImp_().pvtRegionIndex();
|
|
Evaluation bGasEff = rhoGasEff;
|
|
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
|
|
bGasEff /= (FluidSystem::referenceDensity(gasPhaseIdx, pvtRegionIdx) + FluidSystem::referenceDensity(oilPhaseIdx, pvtRegionIdx) * fs.Rv());
|
|
} else {
|
|
bGasEff /= (FluidSystem::referenceDensity(gasPhaseIdx, pvtRegionIdx));
|
|
}
|
|
const Evaluation bSolventEff = rhoSolventEff / solventRefDensity();
|
|
|
|
// copy the unmodified invB factors
|
|
const Evaluation bg = fs.invB(gasPhaseIdx);
|
|
const Evaluation bs = solventInverseFormationVolumeFactor();
|
|
const Evaluation bg_eff = pmisc * bGasEff + (1.0 - pmisc) * bg;
|
|
const Evaluation bs_eff = pmisc * bSolventEff + (1.0 - pmisc) * bs;
|
|
|
|
// set the densities
|
|
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
|
|
fs.setDensity(gasPhaseIdx,
|
|
bg_eff
|
|
*(FluidSystem::referenceDensity(gasPhaseIdx, pvtRegionIdx)
|
|
+ FluidSystem::referenceDensity(oilPhaseIdx, pvtRegionIdx)*fs.Rv()));
|
|
} else {
|
|
fs.setDensity(gasPhaseIdx,
|
|
bg_eff
|
|
*FluidSystem::referenceDensity(gasPhaseIdx, pvtRegionIdx));
|
|
}
|
|
solventDensity_ = bs_eff*solventRefDensity();
|
|
|
|
// set the mobility
|
|
Evaluation& mobg = asImp_().mobility_[gasPhaseIdx];
|
|
muGasEff = bg_eff / (pmisc * bGasEff / muGasEff + (1.0 - pmisc) * bg / muGas);
|
|
mobg *= muGas / muGasEff;
|
|
|
|
// Update viscosity of solvent
|
|
solventViscosity_ = bs_eff / (pmisc * bSolventEff / muSolventEff + (1.0 - pmisc) * bs / muSolvent);
|
|
|
|
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
|
|
Evaluation rhoOilEff = 0.0;
|
|
if (std::abs(muOilPow.value() - muSolventPow.value()) < cutOff) {
|
|
rhoOilEff = ((1.0 - tlMixParamRho) * rhoOil) + (tlMixParamRho * rhoMixSolventGasOil);
|
|
}
|
|
else {
|
|
const Evaluation solventOilEffFraction = (muOilPow * (muOilEffPow - muSolventPow)) / (muOilEffPow * (muOilPow - muSolventPow));
|
|
rhoOilEff = (rhoOil * solventOilEffFraction) + (rhoSolvent * (1.0 - solventOilEffFraction));
|
|
}
|
|
const Evaluation bOilEff = rhoOilEff / (FluidSystem::referenceDensity(oilPhaseIdx, pvtRegionIdx) + FluidSystem::referenceDensity(gasPhaseIdx, pvtRegionIdx) * fs.Rs());
|
|
const Evaluation bo = fs.invB(oilPhaseIdx);
|
|
const Evaluation bo_eff = pmisc * bOilEff + (1.0 - pmisc) * bo;
|
|
fs.setDensity(oilPhaseIdx,
|
|
bo_eff
|
|
*(FluidSystem::referenceDensity(oilPhaseIdx, pvtRegionIdx)
|
|
+ FluidSystem::referenceDensity(gasPhaseIdx, pvtRegionIdx)*fs.Rs()));
|
|
|
|
// keep the mu*b interpolation
|
|
Evaluation& mobo = asImp_().mobility_[oilPhaseIdx];
|
|
muOilEff = bo_eff / (pmisc * bOilEff / muOilEff + (1.0 - pmisc) * bo / muOil);
|
|
mobo *= muOil / muOilEff;
|
|
}
|
|
}
|
|
|
|
protected:
|
|
Implementation& asImp_()
|
|
{ return *static_cast<Implementation*>(this); }
|
|
|
|
Evaluation hydrocarbonSaturation_;
|
|
Evaluation solventSaturation_;
|
|
Evaluation rsSolw_;
|
|
Evaluation solventDensity_;
|
|
Evaluation solventViscosity_;
|
|
Evaluation solventMobility_;
|
|
Evaluation solventInvFormationVolumeFactor_;
|
|
|
|
Scalar solventRefDensity_;
|
|
};
|
|
|
|
template <class TypeTag>
|
|
class BlackOilSolventIntensiveQuantities<TypeTag, false>
|
|
{
|
|
using Evaluation = GetPropType<TypeTag, Properties::Evaluation>;
|
|
using ElementContext = GetPropType<TypeTag, Properties::ElementContext>;
|
|
using Scalar = GetPropType<TypeTag, Properties::Scalar>;
|
|
|
|
|
|
public:
|
|
void solventPreSatFuncUpdate_(const ElementContext&,
|
|
unsigned,
|
|
unsigned)
|
|
{ }
|
|
|
|
void solventPostSatFuncUpdate_(const ElementContext&,
|
|
unsigned,
|
|
unsigned)
|
|
{ }
|
|
|
|
void solventPvtUpdate_(const ElementContext&,
|
|
unsigned,
|
|
unsigned)
|
|
{ }
|
|
|
|
const Evaluation& solventSaturation() const
|
|
{ throw std::runtime_error("solventSaturation() called but solvents are disabled"); }
|
|
|
|
const Evaluation& rsSolw() const
|
|
{ throw std::runtime_error("rsSolw() called but solvents are disabled"); }
|
|
|
|
const Evaluation& solventDensity() const
|
|
{ throw std::runtime_error("solventDensity() called but solvents are disabled"); }
|
|
|
|
const Evaluation& solventViscosity() const
|
|
{ throw std::runtime_error("solventViscosity() called but solvents are disabled"); }
|
|
|
|
const Evaluation& solventMobility() const
|
|
{ throw std::runtime_error("solventMobility() called but solvents are disabled"); }
|
|
|
|
const Evaluation& solventInverseFormationVolumeFactor() const
|
|
{ throw std::runtime_error("solventInverseFormationVolumeFactor() called but solvents are disabled"); }
|
|
|
|
const Scalar& solventRefDensity() const
|
|
{ throw std::runtime_error("solventRefDensity() called but solvents are disabled"); }
|
|
};
|
|
|
|
/*!
|
|
* \ingroup BlackOil
|
|
* \class Opm::BlackOilSolventExtensiveQuantities
|
|
*
|
|
* \brief Provides the solvent specific extensive quantities to the generic black-oil
|
|
* module's extensive quantities.
|
|
*/
|
|
template <class TypeTag, bool enableSolventV = getPropValue<TypeTag, Properties::EnableSolvent>()>
|
|
class BlackOilSolventExtensiveQuantities
|
|
{
|
|
using Implementation = GetPropType<TypeTag, Properties::ExtensiveQuantities>;
|
|
|
|
using Scalar = GetPropType<TypeTag, Properties::Scalar>;
|
|
using Evaluation = GetPropType<TypeTag, Properties::Evaluation>;
|
|
using ElementContext = GetPropType<TypeTag, Properties::ElementContext>;
|
|
using IntensiveQuantities = GetPropType<TypeTag, Properties::IntensiveQuantities>;
|
|
using ExtensiveQuantities = GetPropType<TypeTag, Properties::ExtensiveQuantities>;
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using FluidSystem = GetPropType<TypeTag, Properties::FluidSystem>;
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using GridView = GetPropType<TypeTag, Properties::GridView>;
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using Toolbox = MathToolbox<Evaluation>;
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static constexpr unsigned gasPhaseIdx = FluidSystem::gasPhaseIdx;
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static constexpr int dimWorld = GridView::dimensionworld;
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using DimVector = Dune::FieldVector<Scalar, dimWorld>;
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using DimEvalVector = Dune::FieldVector<Evaluation, dimWorld>;
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public:
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/*!
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* \brief Method which calculates the volume flux of the polymer "phase" using the
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* pressure potential gradient of the gas phase and the intrinsic permeability
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*/
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template <class Dummy = bool> // we need to make this method a template to avoid
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// compiler errors if it is not instantiated!
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void updateVolumeFluxPerm(const ElementContext& elemCtx,
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unsigned scvfIdx,
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unsigned timeIdx)
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{
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const auto& gradCalc = elemCtx.gradientCalculator();
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PressureCallback<TypeTag> pressureCallback(elemCtx);
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const auto& scvf = elemCtx.stencil(timeIdx).interiorFace(scvfIdx);
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const auto& faceNormal = scvf.normal();
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unsigned i = scvf.interiorIndex();
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unsigned j = scvf.exteriorIndex();
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// calculate the "raw" pressure gradient
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DimEvalVector solventPGrad;
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pressureCallback.setPhaseIndex(gasPhaseIdx);
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gradCalc.calculateGradient(solventPGrad,
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elemCtx,
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scvfIdx,
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pressureCallback);
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Valgrind::CheckDefined(solventPGrad);
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// correct the pressure gradients by the gravitational acceleration
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if (EWOMS_GET_PARAM(TypeTag, bool, EnableGravity)) {
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// estimate the gravitational acceleration at a given SCV face
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// using the arithmetic mean
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const auto& gIn = elemCtx.problem().gravity(elemCtx, i, timeIdx);
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const auto& gEx = elemCtx.problem().gravity(elemCtx, j, timeIdx);
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const auto& intQuantsIn = elemCtx.intensiveQuantities(i, timeIdx);
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const auto& intQuantsEx = elemCtx.intensiveQuantities(j, timeIdx);
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const auto& posIn = elemCtx.pos(i, timeIdx);
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const auto& posEx = elemCtx.pos(j, timeIdx);
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const auto& posFace = scvf.integrationPos();
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// the distance between the centers of the control volumes
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DimVector distVecIn(posIn);
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DimVector distVecEx(posEx);
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DimVector distVecTotal(posEx);
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distVecIn -= posFace;
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distVecEx -= posFace;
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distVecTotal -= posIn;
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Scalar absDistTotalSquared = distVecTotal.two_norm2();
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// calculate the hydrostatic pressure at the integration point of the face
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auto rhoIn = intQuantsIn.solventDensity();
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auto pStatIn = - rhoIn*(gIn*distVecIn);
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// the quantities on the exterior side of the face do not influence the
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// result for the TPFA scheme, so they can be treated as scalar values.
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Scalar rhoEx = Toolbox::value(intQuantsEx.solventDensity());
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Scalar pStatEx = - rhoEx*(gEx*distVecEx);
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// compute the hydrostatic gradient between the two control volumes (this
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// gradient exhibitis the same direction as the vector between the two
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// control volume centers and the length (pStaticExterior -
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// pStaticInterior)/distanceInteriorToExterior
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DimEvalVector f(distVecTotal);
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f *= (pStatEx - pStatIn)/absDistTotalSquared;
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// calculate the final potential gradient
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for (unsigned dimIdx = 0; dimIdx < dimWorld; ++dimIdx) {
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solventPGrad[dimIdx] += f[dimIdx];
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if (!isfinite(solventPGrad[dimIdx]))
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throw NumericalProblem("Non-finite potential gradient for solvent 'phase'");
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}
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}
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// determine the upstream and downstream DOFs
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Evaluation solventPGradNormal = 0.0;
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for (unsigned dimIdx = 0; dimIdx < faceNormal.size(); ++dimIdx)
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solventPGradNormal += solventPGrad[dimIdx]*faceNormal[dimIdx];
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if (solventPGradNormal > 0) {
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solventUpstreamDofIdx_ = j;
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solventDownstreamDofIdx_ = i;
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}
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else {
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solventUpstreamDofIdx_ = i;
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solventDownstreamDofIdx_ = j;
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}
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const auto& up = elemCtx.intensiveQuantities(solventUpstreamDofIdx_, timeIdx);
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// this is also slightly hacky because it assumes that the derivative of the
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// flux between two DOFs only depends on the primary variables in the
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// upstream direction. For non-TPFA flux approximation schemes, this is not
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// true...
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if (solventUpstreamDofIdx_ == i)
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solventVolumeFlux_ = solventPGradNormal*up.solventMobility();
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else
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solventVolumeFlux_ = solventPGradNormal*scalarValue(up.solventMobility());
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}
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/*!
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* \brief Method which calculates the volume flux of the polymer "phase" using the
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* gas pressure potential difference between cells and transmissibilities
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*/
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template <class Dummy = bool> // we need to make this method a template to avoid
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// compiler errors if it is not instantiated!
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void updateVolumeFluxTrans(const ElementContext& elemCtx,
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unsigned scvfIdx,
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unsigned timeIdx)
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{
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const ExtensiveQuantities& extQuants = asImp_();
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unsigned interiorDofIdx = extQuants.interiorIndex();
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unsigned exteriorDofIdx = extQuants.exteriorIndex();
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assert(interiorDofIdx != exteriorDofIdx);
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const auto& intQuantsIn = elemCtx.intensiveQuantities(interiorDofIdx, timeIdx);
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const auto& intQuantsEx = elemCtx.intensiveQuantities(exteriorDofIdx, timeIdx);
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unsigned I = elemCtx.globalSpaceIndex(interiorDofIdx, timeIdx);
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unsigned J = elemCtx.globalSpaceIndex(exteriorDofIdx, timeIdx);
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Scalar thpres = elemCtx.problem().thresholdPressure(I, J);
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Scalar trans = elemCtx.problem().transmissibility(elemCtx, interiorDofIdx, exteriorDofIdx);
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Scalar g = elemCtx.problem().gravity()[dimWorld - 1];
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Scalar zIn = elemCtx.problem().dofCenterDepth(elemCtx, interiorDofIdx, timeIdx);
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Scalar zEx = elemCtx.problem().dofCenterDepth(elemCtx, exteriorDofIdx, timeIdx);
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Scalar distZ = zIn - zEx;
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const Evaluation& rhoIn = intQuantsIn.solventDensity();
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Scalar rhoEx = Toolbox::value(intQuantsEx.solventDensity());
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const Evaluation& rhoAvg = rhoIn*0.5 + rhoEx*0.5;
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const Evaluation& pressureInterior = intQuantsIn.fluidState().pressure(gasPhaseIdx);
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Evaluation pressureExterior = Toolbox::value(intQuantsEx.fluidState().pressure(gasPhaseIdx));
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pressureExterior += distZ*g*rhoAvg;
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Evaluation pressureDiffSolvent = pressureExterior - pressureInterior;
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if (std::abs(scalarValue(pressureDiffSolvent)) > thpres) {
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if (pressureDiffSolvent < 0.0)
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pressureDiffSolvent += thpres;
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else
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pressureDiffSolvent -= thpres;
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}
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else
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pressureDiffSolvent = 0.0;
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if (pressureDiffSolvent > 0.0) {
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solventUpstreamDofIdx_ = exteriorDofIdx;
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solventDownstreamDofIdx_ = interiorDofIdx;
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}
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else if (pressureDiffSolvent < 0.0) {
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solventUpstreamDofIdx_ = interiorDofIdx;
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solventDownstreamDofIdx_ = exteriorDofIdx;
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}
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else {
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// pressure potential gradient is zero; force consistent upstream and
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// downstream indices over the intersection regardless of the side which it
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// is looked at.
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solventUpstreamDofIdx_ = std::min(interiorDofIdx, exteriorDofIdx);
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solventDownstreamDofIdx_ = std::max(interiorDofIdx, exteriorDofIdx);
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solventVolumeFlux_ = 0.0;
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return;
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}
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Scalar faceArea = elemCtx.stencil(timeIdx).interiorFace(scvfIdx).area();
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const IntensiveQuantities& up = elemCtx.intensiveQuantities(solventUpstreamDofIdx_, timeIdx);
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if (solventUpstreamDofIdx_ == interiorDofIdx)
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solventVolumeFlux_ =
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up.solventMobility()
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*(-trans/faceArea)
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*pressureDiffSolvent;
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else
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solventVolumeFlux_ =
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scalarValue(up.solventMobility())
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*(-trans/faceArea)
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*pressureDiffSolvent;
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}
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unsigned solventUpstreamIndex() const
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{ return solventUpstreamDofIdx_; }
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unsigned solventDownstreamIndex() const
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{ return solventDownstreamDofIdx_; }
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const Evaluation& solventVolumeFlux() const
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{ return solventVolumeFlux_; }
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void setSolventVolumeFlux(const Evaluation& solventVolumeFlux)
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{ solventVolumeFlux_ = solventVolumeFlux; }
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private:
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Implementation& asImp_()
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{ return *static_cast<Implementation*>(this); }
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Evaluation solventVolumeFlux_;
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unsigned solventUpstreamDofIdx_;
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unsigned solventDownstreamDofIdx_;
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};
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template <class TypeTag>
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class BlackOilSolventExtensiveQuantities<TypeTag, false>
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{
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using ElementContext = GetPropType<TypeTag, Properties::ElementContext>;
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using Evaluation = GetPropType<TypeTag, Properties::Evaluation>;
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public:
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void updateVolumeFluxPerm(const ElementContext&,
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unsigned,
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unsigned)
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{ }
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void updateVolumeFluxTrans(const ElementContext&,
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unsigned,
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unsigned)
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{ }
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unsigned solventUpstreamIndex() const
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{ throw std::runtime_error("solventUpstreamIndex() called but solvents are disabled"); }
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unsigned solventDownstreamIndex() const
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{ throw std::runtime_error("solventDownstreamIndex() called but solvents are disabled"); }
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const Evaluation& solventVolumeFlux() const
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{ throw std::runtime_error("solventVolumeFlux() called but solvents are disabled"); }
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void setSolventVolumeFlux(const Evaluation& /* solventVolumeFlux */)
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{ throw std::runtime_error("setSolventVolumeFlux() called but solvents are disabled"); }
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};
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} // namespace Opm
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#endif
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