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04d605159f
opm-parser#677 changes the return types for the Deck family of classes. This patch fixes all broken code from that patch set. https://github.com/OPM/opm-parser/pull/677
323 lines
13 KiB
C++
323 lines
13 KiB
C++
/*
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Copyright 2015 Andreas Lauser
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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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#ifndef OPM_THERMAL_GAS_PVT_WRAPPER_HPP
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#define OPM_THERMAL_GAS_PVT_WRAPPER_HPP
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#include <opm/core/props/pvt/PvtInterface.hpp>
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#include <opm/common/ErrorMacros.hpp>
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#include <opm/parser/eclipse/EclipseState/EclipseState.hpp>
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#include <opm/parser/eclipse/EclipseState/Tables/GasvisctTable.hpp>
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#include <vector>
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namespace Opm
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{
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/// Class which wraps another (i.e., isothermal) PVT object into one which adds
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/// temperature dependence of gas
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class ThermalGasPvtWrapper : public PvtInterface
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{
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public:
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ThermalGasPvtWrapper()
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{}
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/// extract the quantities needed specify the temperature dependence of the gas
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/// viscosity and density from the deck
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void initFromDeck(std::shared_ptr<const PvtInterface> isothermalPvt,
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Opm::DeckConstPtr deck,
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Opm::EclipseStateConstPtr eclipseState)
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{
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isothermalPvt_ = isothermalPvt;
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auto tables = eclipseState->getTableManager();
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int numRegions;
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if (deck->hasKeyword("PVTG"))
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numRegions = tables->getPvtgTables().size();
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else if (deck->hasKeyword("PVDG"))
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numRegions = tables->getPvdgTables().size();
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else
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OPM_THROW(std::runtime_error, "Gas phase was not initialized using a known way");
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// viscosity
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if (deck->hasKeyword("GASVISCT")) {
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gasvisctTables_ = &tables->getGasvisctTables();
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assert(int(gasvisctTables_->size()) == numRegions);
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static_cast<void>(numRegions); //Silence compiler warning
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gasCompIdx_ = deck->getKeyword("GCOMPIDX").getRecord(0).getItem("GAS_COMPONENT_INDEX").get< int >(0) - 1;
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gasvisctColumnName_ = "Viscosity"+std::to_string(static_cast<long long>(gasCompIdx_));
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}
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// density
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if (deck->hasKeyword("TREF")) {
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tref_ = deck->getKeyword("TREF").getRecord(0).getItem("TEMPERATURE").getSIDouble(0);
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}
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}
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virtual void mu(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* T,
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const double* z,
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double* output_mu) const
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{
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if (gasvisctTables_)
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// TODO: temperature dependence for viscosity depending on z
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OPM_THROW(std::runtime_error,
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"temperature dependent viscosity as a function of z "
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"is not yet implemented!");
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// compute the isothermal viscosity
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isothermalPvt_->mu(n, pvtRegionIdx, p, T, z, output_mu);
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}
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virtual void mu(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* T,
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const double* r,
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double* output_mu,
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double* output_dmudp,
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double* output_dmudr) const
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{
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if (gasvisctTables_ != 0) {
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for (int i = 0; i < n; ++i) {
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// temperature dependence of the gas phase. this assumes that the gas
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// component index has been set properly, and it also looses the
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// pressure dependence of gas. (This does not make much sense, but it
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// seems to be what the documentation for the GASVISCT keyword in the
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// RM says.)
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int regionIdx = getPvtRegionIndex_(pvtRegionIdx, i);
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double muGasvisct;
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{
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const GasvisctTable& gasvisctTable = gasvisctTables_->getTable<GasvisctTable>(regionIdx);
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muGasvisct = gasvisctTable.evaluate(gasvisctColumnName_, T[i]);
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}
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output_mu[i] = muGasvisct;
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output_dmudp[i] = 0.0;
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output_dmudr[i] = 0.0;
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// TODO (?): derivative of gas viscosity w.r.t. temperature.
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}
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}
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else {
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// compute the isothermal viscosity and its derivatives
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isothermalPvt_->mu(n, pvtRegionIdx, p, T, r, output_mu, output_dmudp, output_dmudr);
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}
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}
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virtual void mu(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* T,
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const double* r,
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const PhasePresence* cond,
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double* output_mu,
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double* output_dmudp,
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double* output_dmudr) const
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{
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if (gasvisctTables_ != 0) {
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for (int i = 0; i < n; ++i) {
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// temperature dependence of the gas phase. this assumes that the gas
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// component index has been set properly, and it also looses the
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// pressure dependence of gas. (This does not make much sense, but it
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// seems to be what the documentation for the GASVISCT keyword in the
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// RM says.)
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int regionIdx = getPvtRegionIndex_(pvtRegionIdx, i);
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double muGasvisct;
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{
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const GasvisctTable& gasvisctTable = gasvisctTables_->getTable<GasvisctTable>(regionIdx);
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muGasvisct = gasvisctTable.evaluate(gasvisctColumnName_, T[i]);
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}
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output_mu[i] = muGasvisct;
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output_dmudp[i] = 0.0;
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output_dmudr[i] = 0.0;
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// TODO (?): derivative of gas viscosity w.r.t. temperature.
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}
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}
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else {
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// compute the isothermal viscosity and its derivatives
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isothermalPvt_->mu(n, pvtRegionIdx, p, T, r, cond, output_mu, output_dmudp, output_dmudr);
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}
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}
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virtual void B(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* T,
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const double* z,
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double* output_B) const
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{
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// isothermal case
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isothermalPvt_->B(n, pvtRegionIdx, p, T, z, output_B);
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if (tref_ > 0.0) {
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// the Eclipse TD/RM do not explicitly specify the relation of the gas
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// density and the temperature, but equation (69.49) (for Eclipse 2011.1)
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// implies that the temperature dependence of the gas phase is rho(T, p) =
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// rho(tref_, p)/tref_*T ...
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for (int i = 0; i < n; ++i) {
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double alpha = tref_/T[i];
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output_B[i] *= alpha;
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}
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}
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}
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virtual void dBdp(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* T,
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const double* z,
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double* output_B,
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double* output_dBdp) const
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{
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isothermalPvt_->dBdp(n, pvtRegionIdx, p, T, z, output_B, output_dBdp);
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if (tref_ > 0.0) {
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// the Eclipse TD/RM do not explicitly specify the relation of the gas
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// density and the temperature, but equation (69.49) (for Eclipse 2011.1)
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// implies that the temperature dependence of the gas phase is rho(T, p) =
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// rho(tref_, p)/tref_*T ...
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for (int i = 0; i < n; ++i) {
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double alpha = tref_/T[i];
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output_B[i] *= alpha;
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output_dBdp[i] *= alpha;
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}
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}
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}
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virtual void b(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* T,
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const double* r,
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double* output_b,
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double* output_dbdp,
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double* output_dbdr) const
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{
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isothermalPvt_->b(n, pvtRegionIdx, p, T, r, output_b, output_dbdp, output_dbdr);
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if (tref_ > 0.0) {
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// the Eclipse TD/RM do not explicitly specify the relation of the gas
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// density and the temperature, but equation (69.49) (for Eclipse 2011.1)
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// implies that the temperature dependence of the gas phase is rho(T, p) =
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// rho(tref_, p)/tref_*T ...
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for (int i = 0; i < n; ++i) {
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double alpha = T[i]/tref_;
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output_b[i] *= alpha;
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output_dbdp[i] *= alpha;
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output_dbdr[i] *= alpha;
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}
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}
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}
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virtual void b(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* T,
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const double* r,
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const PhasePresence* cond,
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double* output_b,
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double* output_dbdp,
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double* output_dbdr) const
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{
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isothermalPvt_->b(n, pvtRegionIdx, p, T, r, cond, output_b, output_dbdp, output_dbdr);
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if (tref_ > 0.0) {
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// the Eclipse TD/RM do not explicitly specify the relation of the gas
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// density and the temperature, but equation (69.49) (for Eclipse 2011.1)
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// implies that the temperature dependence of the gas phase is rho(T, p) =
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// rho(tref_, p)/tref_*T ...
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for (int i = 0; i < n; ++i) {
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double alpha = T[i]/tref_;
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output_b[i] *= alpha;
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output_dbdp[i] *= alpha;
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output_dbdr[i] *= alpha;
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}
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}
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}
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virtual void rsSat(const int n,
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const int* pvtRegionIdx,
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const double* p,
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double* output_rsSat,
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double* output_drsSatdp) const
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{
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isothermalPvt_->rsSat(n, pvtRegionIdx, p, output_rsSat, output_drsSatdp);
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}
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virtual void rvSat(const int n,
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const int* pvtRegionIdx,
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const double* p,
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double* output_rvSat,
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double* output_drvSatdp) const
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{
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isothermalPvt_->rvSat(n, pvtRegionIdx, p, output_rvSat, output_drvSatdp);
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}
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virtual void R(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* z,
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double* output_R) const
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{
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isothermalPvt_->R(n, pvtRegionIdx, p, z, output_R);
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}
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virtual void dRdp(const int n,
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const int* pvtRegionIdx,
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const double* p,
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const double* z,
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double* output_R,
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double* output_dRdp) const
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{
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isothermalPvt_->dRdp(n, pvtRegionIdx, p, z, output_R, output_dRdp);
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}
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private:
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int getPvtRegionIndex_(const int* pvtRegionIdx, int cellIdx) const
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{
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if (!pvtRegionIdx)
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return 0;
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return pvtRegionIdx[cellIdx];
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}
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// the PVT propertied for the isothermal case
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std::shared_ptr<const PvtInterface> isothermalPvt_;
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// The PVT properties needed for temperature dependence of the viscosity. We need
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// to store one value per PVT region.
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const TableContainer* gasvisctTables_;
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std::string gasvisctColumnName_;
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int gasCompIdx_;
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// The PVT properties needed for temperature dependence of the density.
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double tref_;
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};
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}
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#endif
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