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1005 lines
41 KiB
C++
1005 lines
41 KiB
C++
/*
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Copyright 2013 SINTEF ICT, Applied Mathematics.
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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 3 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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*/
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#include <config.h>
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#include <opm/autodiff/BlackoilPropsAdFromDeck.hpp>
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#include <opm/autodiff/AutoDiffHelpers.hpp>
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#include <opm/core/props/BlackoilPropertiesInterface.hpp>
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#include <opm/core/props/BlackoilPhases.hpp>
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#include <opm/core/props/pvt/SinglePvtInterface.hpp>
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#include <opm/core/props/pvt/SinglePvtConstCompr.hpp>
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#include <opm/core/props/pvt/SinglePvtDead.hpp>
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#include <opm/core/props/pvt/SinglePvtDeadSpline.hpp>
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#include <opm/core/props/pvt/SinglePvtLiveOil.hpp>
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#include <opm/core/props/pvt/SinglePvtLiveGas.hpp>
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#include <opm/core/utility/ErrorMacros.hpp>
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#include <opm/core/utility/Units.hpp>
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#include <opm/parser/eclipse/Deck/Deck.hpp>
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#include <opm/parser/eclipse/Utility/PvdoTable.hpp>
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#include <opm/parser/eclipse/Utility/PvtgTable.hpp>
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#include <opm/parser/eclipse/Utility/PvdcoTable.hpp>
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namespace Opm
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{
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// Making these typedef to make the code more readable.
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typedef BlackoilPropsAdFromDeck::ADB ADB;
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typedef BlackoilPropsAdFromDeck::V V;
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typedef Eigen::Array<double, Eigen::Dynamic, Eigen::Dynamic, Eigen::RowMajor> Block;
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enum { Aqua = BlackoilPhases::Aqua,
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Liquid = BlackoilPhases::Liquid,
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Vapour = BlackoilPhases::Vapour };
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/// Constructor wrapping an opm-core black oil interface.
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BlackoilPropsAdFromDeck::BlackoilPropsAdFromDeck(const EclipseGridParser& deck,
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const UnstructuredGrid& grid,
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const bool init_rock)
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{
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if (init_rock){
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rock_.init(deck, grid);
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}
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const int samples = 0;
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const int region_number = 0;
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phase_usage_ = phaseUsageFromDeck(deck);
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// Surface densities. Accounting for different orders in eclipse and our code.
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if (deck.hasField("DENSITY")) {
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const std::vector<double>& d = deck.getDENSITY().densities_[region_number];
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enum { ECL_oil = 0, ECL_water = 1, ECL_gas = 2 };
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if (phase_usage_.phase_used[Aqua]) {
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densities_[phase_usage_.phase_pos[Aqua]] = d[ECL_water];
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}
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if (phase_usage_.phase_used[Vapour]) {
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densities_[phase_usage_.phase_pos[Vapour]] = d[ECL_gas];
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}
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if (phase_usage_.phase_used[Liquid]) {
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densities_[phase_usage_.phase_pos[Liquid]] = d[ECL_oil];
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}
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} else {
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OPM_THROW(std::runtime_error, "Input is missing DENSITY\n");
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}
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// Set the properties.
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props_.resize(phase_usage_.num_phases);
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// Water PVT
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if (phase_usage_.phase_used[Aqua]) {
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if (deck.hasField("PVTW")) {
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props_[phase_usage_.phase_pos[Aqua]].reset(new SinglePvtConstCompr(deck.getPVTW().pvtw_));
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} else {
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// Eclipse 100 default.
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props_[phase_usage_.phase_pos[Aqua]].reset(new SinglePvtConstCompr(0.5*Opm::prefix::centi*Opm::unit::Poise));
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}
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}
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// Oil PVT
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if (phase_usage_.phase_used[Liquid]) {
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if (deck.hasField("PVDO")) {
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if (samples > 0) {
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props_[phase_usage_.phase_pos[Liquid]].reset(new SinglePvtDeadSpline(deck.getPVDO().pvdo_, samples));
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} else {
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props_[phase_usage_.phase_pos[Liquid]].reset(new SinglePvtDead(deck.getPVDO().pvdo_));
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}
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} else if (deck.hasField("PVTO")) {
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props_[phase_usage_.phase_pos[Liquid]].reset(new SinglePvtLiveOil(deck.getPVTO().pvto_));
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} else if (deck.hasField("PVCDO")) {
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props_[phase_usage_.phase_pos[Liquid]].reset(new SinglePvtConstCompr(deck.getPVCDO().pvcdo_));
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} else {
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OPM_THROW(std::runtime_error, "Input is missing PVDO, PVTO or PVCDO\n");
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}
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}
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// Gas PVT
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if (phase_usage_.phase_used[Vapour]) {
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if (deck.hasField("PVDG")) {
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if (samples > 0) {
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props_[phase_usage_.phase_pos[Vapour]].reset(new SinglePvtDeadSpline(deck.getPVDG().pvdg_, samples));
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} else {
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props_[phase_usage_.phase_pos[Vapour]].reset(new SinglePvtDead(deck.getPVDG().pvdg_));
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}
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} else if (deck.hasField("PVTG")) {
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props_[phase_usage_.phase_pos[Vapour]].reset(new SinglePvtLiveGas(deck.getPVTG().pvtg_));
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} else {
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OPM_THROW(std::runtime_error, "Input is missing PVDG or PVTG\n");
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}
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}
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SaturationPropsFromDeck<SatFuncGwsegNonuniform>* ptr
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= new SaturationPropsFromDeck<SatFuncGwsegNonuniform>();
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satprops_.reset(ptr);
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ptr->init(deck, grid, -1);
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if (phase_usage_.num_phases != satprops_->numPhases()) {
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OPM_THROW(std::runtime_error, "BlackoilPropsAdFromDeck::BlackoilPropsAdFromDeck() - "
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"Inconsistent number of phases in pvt data (" << phase_usage_.num_phases
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<< ") and saturation-dependent function data (" << satprops_->numPhases() << ").");
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}
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}
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/// Constructor wrapping an opm-core black oil interface.
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BlackoilPropsAdFromDeck::BlackoilPropsAdFromDeck(Opm::DeckConstPtr newParserDeck,
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const UnstructuredGrid& grid,
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const bool init_rock)
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{
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if (init_rock){
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rock_.init(newParserDeck, grid);
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}
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const int region_number = 0;
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phase_usage_ = phaseUsageFromDeck(newParserDeck);
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// Surface densities. Accounting for different orders in eclipse and our code.
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if (newParserDeck->hasKeyword("DENSITY")) {
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const auto keyword = newParserDeck->getKeyword("DENSITY");
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const auto record = keyword->getRecord(region_number);
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enum { ECL_oil = 0, ECL_water = 1, ECL_gas = 2 };
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if (phase_usage_.phase_used[Aqua]) {
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densities_[phase_usage_.phase_pos[Aqua]] = record->getItem("WATER")->getSIDouble(0);
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}
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if (phase_usage_.phase_used[Vapour]) {
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densities_[phase_usage_.phase_pos[Vapour]] = record->getItem("GAS")->getSIDouble(0);
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}
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if (phase_usage_.phase_used[Liquid]) {
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densities_[phase_usage_.phase_pos[Liquid]] = record->getItem("OIL")->getSIDouble(0);
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}
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} else {
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OPM_THROW(std::runtime_error, "Input is missing DENSITY\n");
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}
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// Set the properties.
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props_.resize(phase_usage_.num_phases);
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// Water PVT
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if (phase_usage_.phase_used[Aqua]) {
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if (newParserDeck->hasKeyword("PVTW")) {
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Opm::PvtwTable pvtwTable(newParserDeck->getKeyword("PVTW"), region_number);
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props_[phase_usage_.phase_pos[Aqua]].reset(new SinglePvtConstCompr(pvtwTable));
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} else {
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// Eclipse 100 default.
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props_[phase_usage_.phase_pos[Aqua]].reset(new SinglePvtConstCompr(0.5*Opm::prefix::centi*Opm::unit::Poise));
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}
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}
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// Oil PVT
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if (phase_usage_.phase_used[Liquid]) {
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if (newParserDeck->hasKeyword("PVDO")) {
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Opm::PvdoTable pvdoTable(newParserDeck->getKeyword("PVDO"), region_number);
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props_[phase_usage_.phase_pos[Liquid]].reset(new SinglePvtDead(pvdoTable));
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}
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else if (newParserDeck->hasKeyword("PVTO")) {
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Opm::PvtoTable pvtoTable(newParserDeck->getKeyword("PVTO"), /*tableIdx=*/0);
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props_[phase_usage_.phase_pos[Liquid]].reset(new SinglePvtLiveOil(pvtoTable));
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} else if (newParserDeck->hasKeyword("PVCDO")) {
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Opm::PvdcoTable pvdcoTable(newParserDeck->getKeyword("PVDCO"), region_number);
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props_[phase_usage_.phase_pos[Liquid]].reset(new SinglePvtConstCompr(pvdcoTable));
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} else {
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OPM_THROW(std::runtime_error, "Input is missing PVDO, PVTO or PVCDO\n");
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}
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}
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// Gas PVT
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if (phase_usage_.phase_used[Vapour]) {
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if (newParserDeck->hasKeyword("PVDG")) {
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Opm::PvdoTable pvdgTable(newParserDeck->getKeyword("PVDG"), region_number);
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props_[phase_usage_.phase_pos[Vapour]].reset(new SinglePvtDead(pvdgTable));
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} else if (newParserDeck->hasKeyword("PVTG")) {
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Opm::PvtgTable pvtgTable(newParserDeck->getKeyword("PVTG"), /*tableIdx=*/0);
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props_[phase_usage_.phase_pos[Vapour]].reset(new SinglePvtLiveGas(pvtgTable));
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} else {
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OPM_THROW(std::runtime_error, "Input is missing PVDG or PVTG\n");
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}
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}
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SaturationPropsFromDeck<SatFuncGwsegNonuniform>* ptr
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= new SaturationPropsFromDeck<SatFuncGwsegNonuniform>();
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satprops_.reset(ptr);
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ptr->init(newParserDeck, grid, -1);
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if (phase_usage_.num_phases != satprops_->numPhases()) {
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OPM_THROW(std::runtime_error, "BlackoilPropsAdFromDeck::BlackoilPropsAdFromDeck() - "
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"Inconsistent number of phases in pvt data (" << phase_usage_.num_phases
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<< ") and saturation-dependent function data (" << satprops_->numPhases() << ").");
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}
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}
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////////////////////////////
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// Rock interface //
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////////////////////////////
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/// \return D, the number of spatial dimensions.
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int BlackoilPropsAdFromDeck::numDimensions() const
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{
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return rock_.numDimensions();
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}
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/// \return N, the number of cells.
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int BlackoilPropsAdFromDeck::numCells() const
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{
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return rock_.numCells();
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}
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/// \return Array of N porosity values.
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const double* BlackoilPropsAdFromDeck::porosity() const
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{
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return rock_.porosity();
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}
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/// \return Array of ND^2 permeability values.
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/// The D^2 permeability values for a cell are organized as a matrix,
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/// which is symmetric (so ordering does not matter).
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const double* BlackoilPropsAdFromDeck::permeability() const
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{
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return rock_.permeability();
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}
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////////////////////////////
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// Fluid interface //
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////////////////////////////
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/// \return Number of active phases (also the number of components).
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int BlackoilPropsAdFromDeck::numPhases() const
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{
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return phase_usage_.num_phases;
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}
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/// \return Object describing the active phases.
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PhaseUsage BlackoilPropsAdFromDeck::phaseUsage() const
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{
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return phase_usage_;
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}
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// ------ Density ------
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/// Densities of stock components at surface conditions.
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/// \return Array of 3 density values.
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const double* BlackoilPropsAdFromDeck::surfaceDensity() const
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{
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return densities_;
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}
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// ------ Viscosity ------
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/// Water viscosity.
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/// \param[in] pw Array of n water pressure values.
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/// \param[in] cells Array of n cell indices to be associated with the pressure values.
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/// \return Array of n viscosity values.
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V BlackoilPropsAdFromDeck::muWat(const V& pw,
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const Cells& cells) const
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{
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if (!phase_usage_.phase_used[Water]) {
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OPM_THROW(std::runtime_error, "Cannot call muWat(): water phase not present.");
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}
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const int n = cells.size();
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assert(pw.size() == n);
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V mu(n);
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V dmudp(n);
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V dmudr(n);
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const double* rs = 0;
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props_[phase_usage_.phase_pos[Water]]->mu(n, pw.data(), rs,
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mu.data(), dmudp.data(), dmudr.data());
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return mu;
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}
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/// Oil viscosity.
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/// \param[in] po Array of n oil pressure values.
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/// \param[in] rs Array of n gas solution factor values.
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/// \param[in] cond Array of n taxonomies classifying fluid condition.
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/// \param[in] cells Array of n cell indices to be associated with the pressure values.
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/// \return Array of n viscosity values.
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V BlackoilPropsAdFromDeck::muOil(const V& po,
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const V& rs,
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const std::vector<PhasePresence>& cond,
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const Cells& cells) const
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{
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if (!phase_usage_.phase_used[Oil]) {
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OPM_THROW(std::runtime_error, "Cannot call muOil(): oil phase not present.");
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}
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const int n = cells.size();
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assert(po.size() == n);
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V mu(n);
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V dmudp(n);
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V dmudr(n);
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props_[phase_usage_.phase_pos[Oil]]->mu(n, po.data(), rs.data(), &cond[0],
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mu.data(), dmudp.data(), dmudr.data());
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return mu;
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}
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/// Gas viscosity.
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/// \param[in] pg Array of n gas pressure values.
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/// \param[in] cells Array of n cell indices to be associated with the pressure values.
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/// \return Array of n viscosity values.
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V BlackoilPropsAdFromDeck::muGas(const V& pg,
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const Cells& cells) const
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{
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if (!phase_usage_.phase_used[Gas]) {
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OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
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}
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const int n = cells.size();
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assert(pg.size() == n);
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V mu(n);
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V dmudp(n);
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V dmudr(n);
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const double* rs = 0;
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props_[phase_usage_.phase_pos[Gas]]->mu(n, pg.data(), rs,
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mu.data(), dmudp.data(), dmudr.data());
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return mu;
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}
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/// Gas viscosity.
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/// \param[in] pg Array of n gas pressure values.
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/// \param[in] cells Array of n cell indices to be associated with the pressure values.
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/// \return Array of n viscosity values.
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V BlackoilPropsAdFromDeck::muGas(const V& pg,
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const V& rv,
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const std::vector<PhasePresence>& cond,
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const Cells& cells) const
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{
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if (!phase_usage_.phase_used[Gas]) {
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OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
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}
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const int n = cells.size();
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assert(pg.size() == n);
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V mu(n);
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V dmudp(n);
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V dmudr(n);
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props_[phase_usage_.phase_pos[Gas]]->mu(n, pg.data(), rv.data(),&cond[0],
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mu.data(), dmudp.data(), dmudr.data());
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return mu;
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}
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/// Water viscosity.
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/// \param[in] pw Array of n water pressure values.
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/// \param[in] cells Array of n cell indices to be associated with the pressure values.
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/// \return Array of n viscosity values.
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ADB BlackoilPropsAdFromDeck::muWat(const ADB& pw,
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const Cells& cells) const
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{
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if (!phase_usage_.phase_used[Water]) {
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OPM_THROW(std::runtime_error, "Cannot call muWat(): water phase not present.");
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}
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const int n = cells.size();
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assert(pw.size() == n);
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V mu(n);
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V dmudp(n);
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V dmudr(n);
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const double* rs = 0;
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props_[phase_usage_.phase_pos[Water]]->mu(n, pw.value().data(), rs,
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mu.data(), dmudp.data(), dmudr.data());
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ADB::M dmudp_diag = spdiag(dmudp);
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const int num_blocks = pw.numBlocks();
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std::vector<ADB::M> jacs(num_blocks);
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for (int block = 0; block < num_blocks; ++block) {
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jacs[block] = dmudp_diag * pw.derivative()[block];
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}
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return ADB::function(mu, jacs);
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}
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/// Oil viscosity.
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/// \param[in] po Array of n oil pressure values.
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/// \param[in] rs Array of n gas solution factor values.
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/// \param[in] cond Array of n taxonomies classifying fluid condition.
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/// \param[in] cells Array of n cell indices to be associated with the pressure values.
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/// \return Array of n viscosity values.
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ADB BlackoilPropsAdFromDeck::muOil(const ADB& po,
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const ADB& rs,
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const std::vector<PhasePresence>& cond,
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const Cells& cells) const
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{
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if (!phase_usage_.phase_used[Oil]) {
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OPM_THROW(std::runtime_error, "Cannot call muOil(): oil phase not present.");
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}
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const int n = cells.size();
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assert(po.size() == n);
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V mu(n);
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V dmudp(n);
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V dmudr(n);
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props_[phase_usage_.phase_pos[Oil]]->mu(n, po.value().data(), rs.value().data(),
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&cond[0], mu.data(), dmudp.data(), dmudr.data());
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ADB::M dmudp_diag = spdiag(dmudp);
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ADB::M dmudr_diag = spdiag(dmudr);
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const int num_blocks = po.numBlocks();
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std::vector<ADB::M> jacs(num_blocks);
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for (int block = 0; block < num_blocks; ++block) {
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jacs[block] = dmudp_diag * po.derivative()[block] + dmudr_diag * rs.derivative()[block];
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}
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return ADB::function(mu, jacs);
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}
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/// Gas viscosity.
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/// \param[in] pg Array of n gas pressure values.
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/// \param[in] cells Array of n cell indices to be associated with the pressure values.
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/// \return Array of n viscosity values.
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ADB BlackoilPropsAdFromDeck::muGas(const ADB& pg,
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const Cells& cells) const
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{
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if (!phase_usage_.phase_used[Gas]) {
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OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
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}
|
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const int n = cells.size();
|
|
assert(pg.value().size() == n);
|
|
V mu(n);
|
|
V dmudp(n);
|
|
V dmudr(n);
|
|
const double* rv = 0;
|
|
|
|
props_[phase_usage_.phase_pos[Gas]]->mu(n, pg.value().data(), rv,
|
|
mu.data(), dmudp.data(), dmudr.data());
|
|
|
|
ADB::M dmudp_diag = spdiag(dmudp);
|
|
const int num_blocks = pg.numBlocks();
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = dmudp_diag * pg.derivative()[block];
|
|
}
|
|
return ADB::function(mu, jacs);
|
|
}
|
|
|
|
/// Gas viscosity.
|
|
/// \param[in] pg Array of n gas pressure values.
|
|
/// \param[in] rv Array of n vapor oil/gas ratio
|
|
/// \param[in] cond Array of n taxonomies classifying fluid condition.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n viscosity values.
|
|
ADB BlackoilPropsAdFromDeck::muGas(const ADB& pg,
|
|
const ADB& rv,
|
|
const std::vector<PhasePresence>& cond,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Gas]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(pg.value().size() == n);
|
|
V mu(n);
|
|
V dmudp(n);
|
|
V dmudr(n);
|
|
|
|
props_[phase_usage_.phase_pos[Gas]]->mu(n, pg.value().data(), rv.value().data(),&cond[0],
|
|
mu.data(), dmudp.data(), dmudr.data());
|
|
|
|
ADB::M dmudp_diag = spdiag(dmudp);
|
|
ADB::M dmudr_diag = spdiag(dmudr);
|
|
const int num_blocks = pg.numBlocks();
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = dmudp_diag * pg.derivative()[block] + dmudr_diag * rv.derivative()[block];
|
|
}
|
|
return ADB::function(mu, jacs);
|
|
}
|
|
|
|
|
|
// ------ Formation volume factor (b) ------
|
|
|
|
// These methods all call the matrix() method, after which the variable
|
|
// (also) called 'matrix' contains, in each row, the A = RB^{-1} matrix for
|
|
// a cell. For three-phase black oil:
|
|
// A = [ bw 0 0
|
|
// 0 bo 0
|
|
// 0 b0*rs bw ]
|
|
// Where b = B^{-1}.
|
|
// Therefore, we extract the correct diagonal element, and are done.
|
|
// When we need the derivatives (w.r.t. p, since we don't do w.r.t. rs),
|
|
// we also get the following derivative matrix:
|
|
// A = [ dbw 0 0
|
|
// 0 dbo 0
|
|
// 0 db0*rs dbw ]
|
|
// Again, we just extract a diagonal element.
|
|
|
|
/// Water formation volume factor.
|
|
/// \param[in] pw Array of n water pressure values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n formation volume factor values.
|
|
V BlackoilPropsAdFromDeck::bWat(const V& pw,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Water]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call bWat(): water phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(pw.size() == n);
|
|
|
|
V b(n);
|
|
V dbdp(n);
|
|
V dbdr(n);
|
|
const double* rs = 0;
|
|
|
|
props_[phase_usage_.phase_pos[Water]]->b(n, pw.data(), rs,
|
|
b.data(), dbdp.data(), dbdr.data());
|
|
|
|
return b;
|
|
}
|
|
|
|
/// Oil formation volume factor.
|
|
/// \param[in] po Array of n oil pressure values.
|
|
/// \param[in] rs Array of n gas solution factor values.
|
|
/// \param[in] cond Array of n taxonomies classifying fluid condition.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n formation volume factor values.
|
|
V BlackoilPropsAdFromDeck::bOil(const V& po,
|
|
const V& rs,
|
|
const std::vector<PhasePresence>& cond,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Oil]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call bOil(): oil phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(po.size() == n);
|
|
|
|
V b(n);
|
|
V dbdp(n);
|
|
V dbdr(n);
|
|
|
|
props_[phase_usage_.phase_pos[Oil]]->b(n, po.data(), rs.data(), &cond[0],
|
|
b.data(), dbdp.data(), dbdr.data());
|
|
|
|
return b;
|
|
}
|
|
|
|
/// Gas formation volume factor.
|
|
/// \param[in] pg Array of n gas pressure values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n formation volume factor values.
|
|
V BlackoilPropsAdFromDeck::bGas(const V& pg,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Gas]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call bGas(): gas phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(pg.size() == n);
|
|
|
|
V b(n);
|
|
V dbdp(n);
|
|
V dbdr(n);
|
|
const double* rs = 0;
|
|
|
|
props_[phase_usage_.phase_pos[Gas]]->b(n, pg.data(), rs,
|
|
b.data(), dbdp.data(), dbdr.data());
|
|
|
|
return b;
|
|
}
|
|
|
|
/// Gas formation volume factor.
|
|
/// \param[in] pg Array of n gas pressure values.
|
|
/// \param[in] rv Array of n vapor oil/gas ratio
|
|
/// \param[in] cond Array of n objects, each specifying which phases are present with non-zero saturation in a cell.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n formation volume factor values.
|
|
V BlackoilPropsAdFromDeck::bGas(const V& pg,
|
|
const V& rv,
|
|
const std::vector<PhasePresence>& cond,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Gas]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(pg.size() == n);
|
|
|
|
V b(n);
|
|
V dbdp(n);
|
|
V dbdr(n);
|
|
|
|
props_[phase_usage_.phase_pos[Gas]]->b(n, pg.data(), rv.data(), &cond[0],
|
|
b.data(), dbdp.data(), dbdr.data());
|
|
|
|
return b;
|
|
}
|
|
|
|
/// Water formation volume factor.
|
|
/// \param[in] pw Array of n water pressure values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n formation volume factor values.
|
|
ADB BlackoilPropsAdFromDeck::bWat(const ADB& pw,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Water]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call muWat(): water phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(pw.size() == n);
|
|
|
|
V b(n);
|
|
V dbdp(n);
|
|
V dbdr(n);
|
|
const double* rs = 0;
|
|
|
|
props_[phase_usage_.phase_pos[Water]]->b(n, pw.value().data(), rs,
|
|
b.data(), dbdp.data(), dbdr.data());
|
|
|
|
ADB::M dbdp_diag = spdiag(dbdp);
|
|
const int num_blocks = pw.numBlocks();
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = dbdp_diag * pw.derivative()[block];
|
|
}
|
|
return ADB::function(b, jacs);
|
|
}
|
|
|
|
/// Oil formation volume factor.
|
|
/// \param[in] po Array of n oil pressure values.
|
|
/// \param[in] rs Array of n gas solution factor values.
|
|
/// \param[in] cond Array of n taxonomies classifying fluid condition.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n formation volume factor values.
|
|
ADB BlackoilPropsAdFromDeck::bOil(const ADB& po,
|
|
const ADB& rs,
|
|
const std::vector<PhasePresence>& cond,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Oil]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call muOil(): oil phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(po.size() == n);
|
|
|
|
V b(n);
|
|
V dbdp(n);
|
|
V dbdr(n);
|
|
|
|
props_[phase_usage_.phase_pos[Oil]]->b(n, po.value().data(), rs.value().data(),
|
|
&cond[0], b.data(), dbdp.data(), dbdr.data());
|
|
|
|
ADB::M dbdp_diag = spdiag(dbdp);
|
|
ADB::M dbdr_diag = spdiag(dbdr);
|
|
const int num_blocks = po.numBlocks();
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = dbdp_diag * po.derivative()[block] + dbdr_diag * rs.derivative()[block];
|
|
}
|
|
return ADB::function(b, jacs);
|
|
}
|
|
|
|
/// Gas formation volume factor.
|
|
/// \param[in] pg Array of n gas pressure values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n formation volume factor values.
|
|
ADB BlackoilPropsAdFromDeck::bGas(const ADB& pg,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Gas]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(pg.size() == n);
|
|
|
|
V b(n);
|
|
V dbdp(n);
|
|
V dbdr(n);
|
|
const double* rv = 0;
|
|
|
|
props_[phase_usage_.phase_pos[Gas]]->b(n, pg.value().data(), rv,
|
|
b.data(), dbdp.data(), dbdr.data());
|
|
|
|
ADB::M dbdp_diag = spdiag(dbdp);
|
|
const int num_blocks = pg.numBlocks();
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = dbdp_diag * pg.derivative()[block];
|
|
}
|
|
return ADB::function(b, jacs);
|
|
}
|
|
|
|
/// Gas formation volume factor.
|
|
/// \param[in] pg Array of n gas pressure values.
|
|
/// \param[in] rv Array of n vapor oil/gas ratio
|
|
/// \param[in] cond Array of n objects, each specifying which phases are present with non-zero saturation in a cell.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n formation volume factor values.
|
|
ADB BlackoilPropsAdFromDeck::bGas(const ADB& pg,
|
|
const ADB& rv,
|
|
const std::vector<PhasePresence>& cond,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Gas]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call muGas(): gas phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(pg.size() == n);
|
|
|
|
V b(n);
|
|
V dbdp(n);
|
|
V dbdr(n);
|
|
|
|
props_[phase_usage_.phase_pos[Gas]]->b(n, pg.value().data(), rv.value().data(), &cond[0],
|
|
b.data(), dbdp.data(), dbdr.data());
|
|
|
|
ADB::M dbdp_diag = spdiag(dbdp);
|
|
ADB::M dmudr_diag = spdiag(dbdr);
|
|
const int num_blocks = pg.numBlocks();
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = dbdp_diag * pg.derivative()[block] + dmudr_diag * rv.derivative()[block];;
|
|
}
|
|
return ADB::function(b, jacs);
|
|
}
|
|
|
|
|
|
|
|
// ------ Rs bubble point curve ------
|
|
|
|
/// Bubble point curve for Rs as function of oil pressure.
|
|
/// \param[in] po Array of n oil pressure values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n bubble point values for Rs.
|
|
V BlackoilPropsAdFromDeck::rsSat(const V& po,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Oil]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call rsMax(): oil phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(po.size() == n);
|
|
V rbub(n);
|
|
V drbubdp(n);
|
|
props_[Oil]->rsSat(n, po.data(), rbub.data(), drbubdp.data());
|
|
return rbub;
|
|
}
|
|
|
|
/// Bubble point curve for Rs as function of oil pressure.
|
|
/// \param[in] po Array of n oil pressure values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n bubble point values for Rs.
|
|
ADB BlackoilPropsAdFromDeck::rsSat(const ADB& po,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Oil]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call rsMax(): oil phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(po.size() == n);
|
|
V rbub(n);
|
|
V drbubdp(n);
|
|
props_[Oil]->rsSat(n, po.value().data(), rbub.data(), drbubdp.data());
|
|
ADB::M drbubdp_diag = spdiag(drbubdp);
|
|
const int num_blocks = po.numBlocks();
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = drbubdp_diag * po.derivative()[block];
|
|
}
|
|
return ADB::function(rbub, jacs);
|
|
}
|
|
|
|
// ------ Condensation curve ------
|
|
|
|
/// Condensation curve for Rv as function of oil pressure.
|
|
/// \param[in] po Array of n oil pressure values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n bubble point values for Rs.
|
|
V BlackoilPropsAdFromDeck::rvSat(const V& po,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Gas]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call rvMax(): gas phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(po.size() == n);
|
|
V rv(n);
|
|
V drvdp(n);
|
|
props_[Gas]->rvSat(n, po.data(), rv.data(), drvdp.data());
|
|
return rv;
|
|
}
|
|
|
|
/// Condensation curve for Rv as function of oil pressure.
|
|
/// \param[in] po Array of n oil pressure values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the pressure values.
|
|
/// \return Array of n bubble point values for Rs.
|
|
ADB BlackoilPropsAdFromDeck::rvSat(const ADB& po,
|
|
const Cells& cells) const
|
|
{
|
|
if (!phase_usage_.phase_used[Gas]) {
|
|
OPM_THROW(std::runtime_error, "Cannot call rvMax(): gas phase not present.");
|
|
}
|
|
const int n = cells.size();
|
|
assert(po.size() == n);
|
|
V rv(n);
|
|
V drvdp(n);
|
|
props_[Gas]->rvSat(n, po.value().data(), rv.data(), drvdp.data());
|
|
ADB::M drvdp_diag = spdiag(drvdp);
|
|
const int num_blocks = po.numBlocks();
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = drvdp_diag * po.derivative()[block];
|
|
}
|
|
return ADB::function(rv, jacs);
|
|
}
|
|
|
|
// ------ Relative permeability ------
|
|
|
|
/// Relative permeabilities for all phases.
|
|
/// \param[in] sw Array of n water saturation values.
|
|
/// \param[in] so Array of n oil saturation values.
|
|
/// \param[in] sg Array of n gas saturation values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the saturation values.
|
|
/// \return An std::vector with 3 elements, each an array of n relperm values,
|
|
/// containing krw, kro, krg. Use PhaseIndex for indexing into the result.
|
|
std::vector<V> BlackoilPropsAdFromDeck::relperm(const V& sw,
|
|
const V& so,
|
|
const V& sg,
|
|
const Cells& cells) const
|
|
{
|
|
const int n = cells.size();
|
|
const int np = numPhases();
|
|
Block s_all(n, np);
|
|
if (phase_usage_.phase_used[Water]) {
|
|
assert(sw.size() == n);
|
|
s_all.col(phase_usage_.phase_pos[Water]) = sw;
|
|
}
|
|
if (phase_usage_.phase_used[Oil]) {
|
|
assert(so.size() == n);
|
|
s_all.col(phase_usage_.phase_pos[Oil]) = so;
|
|
}
|
|
if (phase_usage_.phase_used[Gas]) {
|
|
assert(sg.size() == n);
|
|
s_all.col(phase_usage_.phase_pos[Gas]) = sg;
|
|
}
|
|
Block kr(n, np);
|
|
satprops_->relperm(n, s_all.data(), cells.data(), kr.data(), 0);
|
|
std::vector<V> relperms;
|
|
relperms.reserve(3);
|
|
for (int phase = 0; phase < 3; ++phase) {
|
|
if (phase_usage_.phase_used[phase]) {
|
|
relperms.emplace_back(kr.col(phase_usage_.phase_pos[phase]));
|
|
} else {
|
|
relperms.emplace_back();
|
|
}
|
|
}
|
|
return relperms;
|
|
}
|
|
|
|
/// Relative permeabilities for all phases.
|
|
/// \param[in] sw Array of n water saturation values.
|
|
/// \param[in] so Array of n oil saturation values.
|
|
/// \param[in] sg Array of n gas saturation values.
|
|
/// \param[in] cells Array of n cell indices to be associated with the saturation values.
|
|
/// \return An std::vector with 3 elements, each an array of n relperm values,
|
|
/// containing krw, kro, krg. Use PhaseIndex for indexing into the result.
|
|
std::vector<ADB> BlackoilPropsAdFromDeck::relperm(const ADB& sw,
|
|
const ADB& so,
|
|
const ADB& sg,
|
|
const Cells& cells) const
|
|
{
|
|
const int n = cells.size();
|
|
const int np = numPhases();
|
|
Block s_all(n, np);
|
|
if (phase_usage_.phase_used[Water]) {
|
|
assert(sw.value().size() == n);
|
|
s_all.col(phase_usage_.phase_pos[Water]) = sw.value();
|
|
}
|
|
if (phase_usage_.phase_used[Oil]) {
|
|
assert(so.value().size() == n);
|
|
s_all.col(phase_usage_.phase_pos[Oil]) = so.value();
|
|
} else {
|
|
OPM_THROW(std::runtime_error, "BlackoilPropsAdFromDeck::relperm() assumes oil phase is active.");
|
|
}
|
|
if (phase_usage_.phase_used[Gas]) {
|
|
assert(sg.value().size() == n);
|
|
s_all.col(phase_usage_.phase_pos[Gas]) = sg.value();
|
|
}
|
|
Block kr(n, np);
|
|
Block dkr(n, np*np);
|
|
satprops_->relperm(n, s_all.data(), cells.data(), kr.data(), dkr.data());
|
|
const int num_blocks = so.numBlocks();
|
|
std::vector<ADB> relperms;
|
|
relperms.reserve(3);
|
|
typedef const ADB* ADBPtr;
|
|
ADBPtr s[3] = { &sw, &so, &sg };
|
|
for (int phase1 = 0; phase1 < 3; ++phase1) {
|
|
if (phase_usage_.phase_used[phase1]) {
|
|
const int phase1_pos = phase_usage_.phase_pos[phase1];
|
|
std::vector<ADB::M> jacs(num_blocks);
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] = ADB::M(n, s[phase1]->derivative()[block].cols());
|
|
}
|
|
for (int phase2 = 0; phase2 < 3; ++phase2) {
|
|
if (!phase_usage_.phase_used[phase2]) {
|
|
continue;
|
|
}
|
|
const int phase2_pos = phase_usage_.phase_pos[phase2];
|
|
// Assemble dkr1/ds2.
|
|
const int column = phase1_pos + np*phase2_pos; // Recall: Fortran ordering from props_.relperm()
|
|
ADB::M dkr1_ds2_diag = spdiag(dkr.col(column));
|
|
for (int block = 0; block < num_blocks; ++block) {
|
|
jacs[block] += dkr1_ds2_diag * s[phase2]->derivative()[block];
|
|
}
|
|
}
|
|
relperms.emplace_back(ADB::function(kr.col(phase1_pos), jacs));
|
|
} else {
|
|
relperms.emplace_back(ADB::null());
|
|
}
|
|
}
|
|
return relperms;
|
|
}
|
|
|
|
std::vector<ADB> BlackoilPropsAdFromDeck::capPress(const ADB& sw,
|
|
const ADB& so,
|
|
const ADB& sg,
|
|
const Cells& cells) const
|
|
{
|
|
const int numCells = cells.size();
|
|
const int numActivePhases = numPhases();
|
|
const int numBlocks = so.numBlocks();
|
|
|
|
Block activeSat(numCells, numActivePhases);
|
|
if (phase_usage_.phase_used[Water]) {
|
|
assert(sw.value().size() == numCells);
|
|
activeSat.col(phase_usage_.phase_pos[Water]) = sw.value();
|
|
}
|
|
if (phase_usage_.phase_used[Oil]) {
|
|
assert(so.value().size() == numCells);
|
|
activeSat.col(phase_usage_.phase_pos[Oil]) = so.value();
|
|
} else {
|
|
OPM_THROW(std::runtime_error, "BlackoilPropsAdFromDeck::relperm() assumes oil phase is active.");
|
|
}
|
|
if (phase_usage_.phase_used[Gas]) {
|
|
assert(sg.value().size() == numCells);
|
|
activeSat.col(phase_usage_.phase_pos[Gas]) = sg.value();
|
|
}
|
|
|
|
Block pc(numCells, numActivePhases);
|
|
Block dpc(numCells, numActivePhases*numActivePhases);
|
|
satprops_->capPress(numCells, activeSat.data(), cells.data(), pc.data(), dpc.data());
|
|
|
|
std::vector<ADB> adbCapPressures;
|
|
adbCapPressures.reserve(3);
|
|
const ADB* s[3] = { &sw, &so, &sg };
|
|
for (int phase1 = 0; phase1 < 3; ++phase1) {
|
|
if (phase_usage_.phase_used[phase1]) {
|
|
const int phase1_pos = phase_usage_.phase_pos[phase1];
|
|
std::vector<ADB::M> jacs(numBlocks);
|
|
for (int block = 0; block < numBlocks; ++block) {
|
|
jacs[block] = ADB::M(numCells, s[phase1]->derivative()[block].cols());
|
|
}
|
|
for (int phase2 = 0; phase2 < 3; ++phase2) {
|
|
if (!phase_usage_.phase_used[phase2])
|
|
continue;
|
|
const int phase2_pos = phase_usage_.phase_pos[phase2];
|
|
// Assemble dpc1/ds2.
|
|
const int column = phase1_pos + numActivePhases*phase2_pos; // Recall: Fortran ordering from props_.relperm()
|
|
ADB::M dpc1_ds2_diag = spdiag(dpc.col(column));
|
|
for (int block = 0; block < numBlocks; ++block) {
|
|
jacs[block] += dpc1_ds2_diag * s[phase2]->derivative()[block];
|
|
}
|
|
}
|
|
adbCapPressures.emplace_back(ADB::function(pc.col(phase1_pos), jacs));
|
|
} else {
|
|
adbCapPressures.emplace_back(ADB::null());
|
|
}
|
|
}
|
|
return adbCapPressures;
|
|
}
|
|
|
|
} // namespace Opm
|
|
|