OilfieldToolsNet/opm-simulators
4
0
Fork 0
mirror of https://github.com/OPM/opm-simulators.git synced 2024-12-01 05:19:09 -06:00
Code Issues Packages Projects Releases Wiki Activity
194bf9d6af
opm-simulators/ebos/ecloutputblackoilmodule.hh
Bård Skaflestad 9fdc007c07 Apply Full SWATINIT-Like PCOW Rescaling at Restart 
We switch to using the applyRestartSwatInit() member function
instead of directly mutating a data member of the EpsInfo structure.
This way we defer the rescaling to a context with a more complete
view of the changes needed to convey the information to all
components involved.
2023-10-25 11:04:51 +02:00

1567 lines
72 KiB
C++
Raw Blame History

// -*- mode: C++; tab-width: 4; indent-tabs-mode: nil; c-basic-offset: 4 -*-
// vi: set et ts=4 sw=4 sts=4:
/*
This file is part of the Open Porous Media project (OPM).
OPM is free software: you can redistribute it and/or modify
it under the terms of the GNU General Public License as published by
the Free Software Foundation, either version 2 of the License, or
(at your option) any later version.
OPM is distributed in the hope that it will be useful,
but WITHOUT ANY WARRANTY; without even the implied warranty of
MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the
GNU General Public License for more details.
You should have received a copy of the GNU General Public License
along with OPM. If not, see <http://www.gnu.org/licenses/>.
Consult the COPYING file in the top-level source directory of this
module for the precise wording of the license and the list of
copyright holders.
*/
/*!
* \file
* \copydoc Opm::EclOutputBlackOilModule
*/
#ifndef EWOMS_ECL_OUTPUT_BLACK_OIL_MODULE_HH
#define EWOMS_ECL_OUTPUT_BLACK_OIL_MODULE_HH
#include <dune/common/fvector.hh>
#include <ebos/eclgenericoutputblackoilmodule.hh>
#include <opm/common/Exceptions.hpp>
#include <opm/common/TimingMacros.hpp>
#include <opm/common/OpmLog/OpmLog.hpp>
#include <opm/material/common/Valgrind.hpp>
#include <opm/material/fluidmatrixinteractions/EclEpsScalingPoints.hpp>
#include <opm/material/fluidstates/BlackOilFluidState.hpp>
#include <opm/material/fluidsystems/BlackOilFluidSystem.hpp>
#include <opm/models/blackoil/blackoilproperties.hh>
#include <opm/models/discretization/common/fvbaseproperties.hh>
#include <opm/models/utils/parametersystem.hh>
#include <opm/models/utils/propertysystem.hh>
#include <opm/output/data/Cells.hpp>
#include <opm/output/eclipse/EclipseIO.hpp>
#include <opm/output/eclipse/Inplace.hpp>
#include <algorithm>
#include <array>
#include <cassert>
#include <cstddef>
#include <initializer_list>
#include <numeric>
#include <optional>
#include <stdexcept>
#include <string>
#include <tuple>
#include <type_traits>
#include <utility>
#include <vector>
namespace Opm::Properties
{
// create new type tag for the Ecl-output
namespace TTag
{
struct EclOutputBlackOil {
};
} // namespace TTag
template <class TypeTag, class MyTypeTag>
struct ForceDisableFluidInPlaceOutput {
using type = UndefinedProperty;
};
template <class TypeTag>
struct ForceDisableFluidInPlaceOutput<TypeTag, TTag::EclOutputBlackOil> {
static constexpr bool value = false;
};
template <class TypeTag, class MyTypeTag>
struct ForceDisableResvFluidInPlaceOutput {
using type = UndefinedProperty;
};
template <class TypeTag>
struct ForceDisableResvFluidInPlaceOutput<TypeTag, TTag::EclOutputBlackOil> {
static constexpr bool value = false;
};
} // namespace Opm::Properties
namespace Opm
{
// forward declaration
template <class TypeTag>
class EcfvDiscretization;
/*!
* \ingroup EclBlackOilSimulator
*
* \brief Output module for the results black oil model writing in
* ECL binary format.
*/
template <class TypeTag>
class EclOutputBlackOilModule : public EclGenericOutputBlackoilModule<GetPropType<TypeTag, Properties::FluidSystem>,
GetPropType<TypeTag, Properties::Scalar>>
{
using Simulator = GetPropType<TypeTag, Properties::Simulator>;
using Discretization = GetPropType<TypeTag, Properties::Discretization>;
using Scalar = GetPropType<TypeTag, Properties::Scalar>;
using Evaluation = GetPropType<TypeTag, Properties::Evaluation>;
using ElementContext = GetPropType<TypeTag, Properties::ElementContext>;
using MaterialLaw = GetPropType<TypeTag, Properties::MaterialLaw>;
using MaterialLawParams = GetPropType<TypeTag, Properties::MaterialLawParams>;
using IntensiveQuantities = GetPropType<TypeTag, Properties::IntensiveQuantities>;
using FluidSystem = GetPropType<TypeTag, Properties::FluidSystem>;
using GridView = GetPropType<TypeTag, Properties::GridView>;
using Element = typename GridView::template Codim<0>::Entity;
using ElementIterator = typename GridView::template Codim<0>::Iterator;
using BaseType = EclGenericOutputBlackoilModule<FluidSystem, Scalar>;
using Indices = GetPropType<TypeTag, Properties::Indices>;
enum { conti0EqIdx = Indices::conti0EqIdx };
enum { numPhases = FluidSystem::numPhases };
enum { oilPhaseIdx = FluidSystem::oilPhaseIdx };
enum { gasPhaseIdx = FluidSystem::gasPhaseIdx };
enum { waterPhaseIdx = FluidSystem::waterPhaseIdx };
enum { gasCompIdx = FluidSystem::gasCompIdx };
enum { oilCompIdx = FluidSystem::oilCompIdx };
enum { waterCompIdx = FluidSystem::waterCompIdx };
enum { enableEnergy = getPropValue<TypeTag, Properties::EnableEnergy>() };
public:
template <class CollectDataToIORankType>
EclOutputBlackOilModule(const Simulator& simulator,
const CollectDataToIORankType& collectToIORank)
: BaseType(simulator.vanguard().eclState(),
simulator.vanguard().schedule(),
simulator.vanguard().summaryConfig(),
simulator.vanguard().summaryState(),
getPropValue<TypeTag, Properties::EnableEnergy>(),
getPropValue<TypeTag, Properties::EnableTemperature>(),
getPropValue<TypeTag, Properties::EnableMech>(),
getPropValue<TypeTag, Properties::EnableSolvent>(),
getPropValue<TypeTag, Properties::EnablePolymer>(),
getPropValue<TypeTag, Properties::EnableFoam>(),
getPropValue<TypeTag, Properties::EnableBrine>(),
getPropValue<TypeTag, Properties::EnableSaltPrecipitation>(),
getPropValue<TypeTag, Properties::EnableExtbo>(),
getPropValue<TypeTag, Properties::EnableMICP>())
, simulator_(simulator)
{
for (auto& region_pair : this->regions_) {
this->createLocalRegion_(region_pair.second);
}
auto isCartIdxOnThisRank = [&collectToIORank](const int idx) {
return collectToIORank.isCartIdxOnThisRank(idx);
};
this->setupBlockData(isCartIdxOnThisRank);
this->forceDisableFipOutput_ =
EWOMS_GET_PARAM(TypeTag, bool, ForceDisableFluidInPlaceOutput);
this->forceDisableFipresvOutput_ =
EWOMS_GET_PARAM(TypeTag, bool, ForceDisableResvFluidInPlaceOutput);
}
/*!
* \brief Register all run-time parameters for the Vtk output module.
*/
static void registerParameters()
{
EWOMS_REGISTER_PARAM(
TypeTag,
bool,
ForceDisableFluidInPlaceOutput,
"Do not print fluid-in-place values after each report step even if requested by the deck.");
EWOMS_REGISTER_PARAM(
TypeTag,
bool,
ForceDisableResvFluidInPlaceOutput,
"Do not print reservoir volumes values after each report step even if requested by the deck.");
}
/*!
* \brief Allocate memory for the scalar fields we would like to
* write to ECL output files
*/
void
allocBuffers(const unsigned bufferSize,
const unsigned reportStepNum,
const bool substep,
const bool log,
const bool isRestart)
{
if (! std::is_same<Discretization, EcfvDiscretization<TypeTag>>::value) {
return;
}
const auto& problem = this->simulator_.problem();
this->doAllocBuffers(bufferSize,
reportStepNum,
substep,
log,
isRestart,
problem.vapparsActive(std::max(simulator_.episodeIndex(), 0)),
problem.materialLawManager()->enableHysteresis(),
problem.tracerModel().numTracers(),
problem.eclWriter()->getOutputNnc().size());
}
void processElementMech(const ElementContext& elemCtx)
{
if constexpr (getPropValue<TypeTag, Properties::EnableMech>()) {
const auto& problem = elemCtx.simulator().problem();
const auto& model = problem.geoMechModel();
for (unsigned dofIdx = 0; dofIdx < elemCtx.numPrimaryDof(/*timeIdx=*/0); ++dofIdx) {
const auto& intQuants = elemCtx.intensiveQuantities(dofIdx, /*timeIdx=*/0);
const auto& fs = intQuants.fluidState();
unsigned globalDofIdx = elemCtx.globalSpaceIndex(dofIdx, /*timeIdx=*/0);
if (!this->mechPotentialForce_.empty()) {
//assume all mechancal tings should be written
this->mechPotentialForce_[globalDofIdx] = model.mechPotentialForce(globalDofIdx);
this->mechPotentialPressForce_[globalDofIdx] = model.mechPotentialPressForce(globalDofIdx);
this->mechPotentialTempForce_[globalDofIdx] = model.mechPotentialTempForce(globalDofIdx);
this->dispX_[globalDofIdx] = model.disp(globalDofIdx, 0);
this->dispY_[globalDofIdx] = model.disp(globalDofIdx, 1);
this->dispZ_[globalDofIdx] = model.disp(globalDofIdx, 2);
this->stressXX_[globalDofIdx] = model.stress(globalDofIdx, 0);
this->stressYY_[globalDofIdx] = model.stress(globalDofIdx, 1);
this->stressZZ_[globalDofIdx] = model.stress(globalDofIdx, 2);
//voight notation
this->stressXY_[globalDofIdx] = model.stress(globalDofIdx, 5);
this->stressXZ_[globalDofIdx] = model.stress(globalDofIdx, 4);
this->stressYZ_[globalDofIdx] = model.stress(globalDofIdx, 3);
this->strainXX_[globalDofIdx] = model.strain(globalDofIdx, 0);
this->strainYY_[globalDofIdx] = model.strain(globalDofIdx, 1);
this->strainZZ_[globalDofIdx] = model.strain(globalDofIdx, 2);
//voight notation
this->strainXY_[globalDofIdx] = model.strain(globalDofIdx, 5);
this->strainXZ_[globalDofIdx] = model.strain(globalDofIdx, 4);
this->strainYZ_[globalDofIdx] = model.strain(globalDofIdx, 3);
this->delstressXX_[globalDofIdx] = model.delstress(globalDofIdx, 0);
this->delstressYY_[globalDofIdx] = model.delstress(globalDofIdx, 1);
this->delstressZZ_[globalDofIdx] = model.delstress(globalDofIdx, 2);
//voight notation
this->delstressXY_[globalDofIdx] = model.delstress(globalDofIdx, 5);
this->delstressXZ_[globalDofIdx] = model.delstress(globalDofIdx, 4);
this->delstressYZ_[globalDofIdx] = model.delstress(globalDofIdx, 3);
}
}
}
}
/*!
* \brief Modify the internal buffers according to the intensive
* quanties relevant for an element
*/
void processElement(const ElementContext& elemCtx)
{
OPM_TIMEBLOCK_LOCAL(processElement);
if (!std::is_same<Discretization, EcfvDiscretization<TypeTag>>::value)
return;
const auto& problem = elemCtx.simulator().problem();
const auto& ebosResid = elemCtx.simulator().model().linearizer().residual();
for (unsigned dofIdx = 0; dofIdx < elemCtx.numPrimaryDof(/*timeIdx=*/0); ++dofIdx) {
const auto& intQuants = elemCtx.intensiveQuantities(dofIdx, /*timeIdx=*/0);
const auto& fs = intQuants.fluidState();
typedef typename std::remove_const<typename std::remove_reference<decltype(fs)>::type>::type FluidState;
unsigned globalDofIdx = elemCtx.globalSpaceIndex(dofIdx, /*timeIdx=*/0);
unsigned pvtRegionIdx = elemCtx.primaryVars(dofIdx, /*timeIdx=*/0).pvtRegionIndex();
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
if (this->saturation_[phaseIdx].empty())
continue;
this->saturation_[phaseIdx][globalDofIdx] = getValue(fs.saturation(phaseIdx));
Valgrind::CheckDefined(this->saturation_[phaseIdx][globalDofIdx]);
}
if (!this->fluidPressure_.empty()) {
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
// Output oil pressure as default
this->fluidPressure_[globalDofIdx] = getValue(fs.pressure(oilPhaseIdx));
} else if (FluidSystem::phaseIsActive(gasPhaseIdx)) {
// Output gas if oil is not present
this->fluidPressure_[globalDofIdx] = getValue(fs.pressure(gasPhaseIdx));
} else {
// Output water if neither oil nor gas is present
this->fluidPressure_[globalDofIdx] = getValue(fs.pressure(waterPhaseIdx));
}
Valgrind::CheckDefined(this->fluidPressure_[globalDofIdx]);
}
if (!this->temperature_.empty()) {
this->temperature_[globalDofIdx] = getValue(fs.temperature(oilPhaseIdx));
Valgrind::CheckDefined(this->temperature_[globalDofIdx]);
}
if (!this->gasDissolutionFactor_.empty()) {
Scalar SoMax = elemCtx.problem().maxOilSaturation(globalDofIdx);
this->gasDissolutionFactor_[globalDofIdx]
= FluidSystem::template saturatedDissolutionFactor<FluidState, Scalar>(
fs, oilPhaseIdx, pvtRegionIdx, SoMax);
Valgrind::CheckDefined(this->gasDissolutionFactor_[globalDofIdx]);
}
if (!this->oilVaporizationFactor_.empty()) {
Scalar SoMax = elemCtx.problem().maxOilSaturation(globalDofIdx);
this->oilVaporizationFactor_[globalDofIdx]
= FluidSystem::template saturatedDissolutionFactor<FluidState, Scalar>(
fs, gasPhaseIdx, pvtRegionIdx, SoMax);
Valgrind::CheckDefined(this->oilVaporizationFactor_[globalDofIdx]);
}
if (!this->gasFormationVolumeFactor_.empty()) {
this->gasFormationVolumeFactor_[globalDofIdx] = 1.0
/ FluidSystem::template inverseFormationVolumeFactor<FluidState, Scalar>(
fs, gasPhaseIdx, pvtRegionIdx);
Valgrind::CheckDefined(this->gasFormationVolumeFactor_[globalDofIdx]);
}
if (!this->saturatedOilFormationVolumeFactor_.empty()) {
this->saturatedOilFormationVolumeFactor_[globalDofIdx] = 1.0
/ FluidSystem::template saturatedInverseFormationVolumeFactor<FluidState, Scalar>(
fs, oilPhaseIdx, pvtRegionIdx);
Valgrind::CheckDefined(this->saturatedOilFormationVolumeFactor_[globalDofIdx]);
}
if (!this->oilSaturationPressure_.empty()) {
this->oilSaturationPressure_[globalDofIdx]
= FluidSystem::template saturationPressure<FluidState, Scalar>(fs, oilPhaseIdx, pvtRegionIdx);
Valgrind::CheckDefined(this->oilSaturationPressure_[globalDofIdx]);
}
if (!this->rs_.empty()) {
this->rs_[globalDofIdx] = getValue(fs.Rs());
Valgrind::CheckDefined(this->rs_[globalDofIdx]);
}
if (!this->rsw_.empty()) {
this->rsw_[globalDofIdx] = getValue(fs.Rsw());
Valgrind::CheckDefined(this->rsw_[globalDofIdx]);
}
if (!this->rv_.empty()) {
this->rv_[globalDofIdx] = getValue(fs.Rv());
Valgrind::CheckDefined(this->rv_[globalDofIdx]);
}
if (!this->pcow_.empty()) {
this->pcow_[globalDofIdx] = getValue(fs.pressure(oilPhaseIdx)) - getValue(fs.pressure(waterPhaseIdx));
Valgrind::CheckDefined(this->pcow_[globalDofIdx]);
}
if (!this->pcog_.empty()) {
this->pcog_[globalDofIdx] = getValue(fs.pressure(gasPhaseIdx)) - getValue(fs.pressure(oilPhaseIdx));
Valgrind::CheckDefined(this->pcog_[globalDofIdx]);
}
if (!this->rvw_.empty()) {
this->rvw_[globalDofIdx] = getValue(fs.Rvw());
Valgrind::CheckDefined(this->rvw_[globalDofIdx]);
}
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
if (this->invB_[phaseIdx].empty())
continue;
this->invB_[phaseIdx][globalDofIdx] = getValue(fs.invB(phaseIdx));
Valgrind::CheckDefined(this->invB_[phaseIdx][globalDofIdx]);
}
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
if (this->density_[phaseIdx].empty())
continue;
this->density_[phaseIdx][globalDofIdx] = getValue(fs.density(phaseIdx));
Valgrind::CheckDefined(this->density_[phaseIdx][globalDofIdx]);
}
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
if (this->viscosity_[phaseIdx].empty())
continue;
if (!this->extboX_.empty() && phaseIdx == oilPhaseIdx)
this->viscosity_[phaseIdx][globalDofIdx] = getValue(intQuants.oilViscosity());
else if (!this->extboX_.empty() && phaseIdx == gasPhaseIdx)
this->viscosity_[phaseIdx][globalDofIdx] = getValue(intQuants.gasViscosity());
else
this->viscosity_[phaseIdx][globalDofIdx] = getValue(fs.viscosity(phaseIdx));
Valgrind::CheckDefined(this->viscosity_[phaseIdx][globalDofIdx]);
}
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
if (this->relativePermeability_[phaseIdx].empty())
continue;
this->relativePermeability_[phaseIdx][globalDofIdx]
= getValue(intQuants.relativePermeability(phaseIdx));
Valgrind::CheckDefined(this->relativePermeability_[phaseIdx][globalDofIdx]);
}
if (!this->drsdtcon_.empty()) {
this->drsdtcon_[globalDofIdx] = problem.drsdtcon(globalDofIdx, elemCtx.simulator().episodeIndex());
}
if (!this->sSol_.empty()) {
this->sSol_[globalDofIdx] = intQuants.solventSaturation().value();
}
if (!this->cPolymer_.empty()) {
this->cPolymer_[globalDofIdx] = intQuants.polymerConcentration().value();
}
if (!this->cFoam_.empty()) {
this->cFoam_[globalDofIdx] = intQuants.foamConcentration().value();
}
if (!this->cSalt_.empty()) {
this->cSalt_[globalDofIdx] = fs.saltConcentration().value();
}
if (!this->pSalt_.empty()) {
this->pSalt_[globalDofIdx] = intQuants.saltSaturation().value();
}
if (!this->permFact_.empty()) {
this->permFact_[globalDofIdx] = intQuants.permFactor().value();
}
if (!this->extboX_.empty()) {
this->extboX_[globalDofIdx] = intQuants.xVolume().value();
}
if (!this->extboY_.empty()) {
this->extboY_[globalDofIdx] = intQuants.yVolume().value();
}
if (!this->extboZ_.empty()) {
this->extboZ_[globalDofIdx] = intQuants.zFraction().value();
}
if (!this->mFracCo2_.empty()) {
const Scalar stdVolOil = getValue(fs.saturation(oilPhaseIdx)) * getValue(fs.invB(oilPhaseIdx))
+ getValue(fs.saturation(gasPhaseIdx)) * getValue(fs.invB(gasPhaseIdx)) * getValue(fs.Rv());
const Scalar stdVolGas = getValue(fs.saturation(gasPhaseIdx)) * getValue(fs.invB(gasPhaseIdx))
* (1.0 - intQuants.yVolume().value())
+ getValue(fs.saturation(oilPhaseIdx)) * getValue(fs.invB(oilPhaseIdx)) * getValue(fs.Rs())
* (1.0 - intQuants.xVolume().value());
const Scalar stdVolCo2 = getValue(fs.saturation(gasPhaseIdx)) * getValue(fs.invB(gasPhaseIdx))
* intQuants.yVolume().value()
+ getValue(fs.saturation(oilPhaseIdx)) * getValue(fs.invB(oilPhaseIdx)) * getValue(fs.Rs())
* intQuants.xVolume().value();
const Scalar rhoO = FluidSystem::referenceDensity(gasPhaseIdx, pvtRegionIdx);
const Scalar rhoG = FluidSystem::referenceDensity(gasPhaseIdx, pvtRegionIdx);
const Scalar rhoCO2 = intQuants.zRefDensity();
const Scalar stdMassTotal = 1.0e-10 + stdVolOil * rhoO + stdVolGas * rhoG + stdVolCo2 * rhoCO2;
this->mFracOil_[globalDofIdx] = stdVolOil * rhoO / stdMassTotal;
this->mFracGas_[globalDofIdx] = stdVolGas * rhoG / stdMassTotal;
this->mFracCo2_[globalDofIdx] = stdVolCo2 * rhoCO2 / stdMassTotal;
}
if (!this->cMicrobes_.empty()) {
this->cMicrobes_[globalDofIdx] = intQuants.microbialConcentration().value();
}
if (!this->cOxygen_.empty()) {
this->cOxygen_[globalDofIdx] = intQuants.oxygenConcentration().value();
}
if (!this->cUrea_.empty()) {
this->cUrea_[globalDofIdx] = 10
* intQuants.ureaConcentration()
.value(); // Reescaling back the urea concentration (see WellInterface_impl.hpp)
}
if (!this->cBiofilm_.empty()) {
this->cBiofilm_[globalDofIdx] = intQuants.biofilmConcentration().value();
}
if (!this->cCalcite_.empty()) {
this->cCalcite_[globalDofIdx] = intQuants.calciteConcentration().value();
}
if (!this->bubblePointPressure_.empty()) {
try {
this->bubblePointPressure_[globalDofIdx]
= getValue(FluidSystem::bubblePointPressure(fs, intQuants.pvtRegionIndex()));
} catch (const NumericalProblem&) {
const auto cartesianIdx = elemCtx.simulator().vanguard().cartesianIndex(globalDofIdx);
this->failedCellsPb_.push_back(cartesianIdx);
}
}
if (!this->dewPointPressure_.empty()) {
try {
this->dewPointPressure_[globalDofIdx]
= getValue(FluidSystem::dewPointPressure(fs, intQuants.pvtRegionIndex()));
} catch (const NumericalProblem&) {
const auto cartesianIdx = elemCtx.simulator().vanguard().cartesianIndex(globalDofIdx);
this->failedCellsPd_.push_back(cartesianIdx);
}
}
if (!this->soMax_.empty())
this->soMax_[globalDofIdx]
= std::max(getValue(fs.saturation(oilPhaseIdx)), problem.maxOilSaturation(globalDofIdx));
if (!this->swMax_.empty())
this->swMax_[globalDofIdx]
= std::max(getValue(fs.saturation(waterPhaseIdx)), problem.maxWaterSaturation(globalDofIdx));
if (!this->minimumOilPressure_.empty())
this->minimumOilPressure_[globalDofIdx]
= std::min(getValue(fs.pressure(oilPhaseIdx)), problem.minOilPressure(globalDofIdx));
if (!this->overburdenPressure_.empty())
this->overburdenPressure_[globalDofIdx] = problem.overburdenPressure(globalDofIdx);
if (!this->rockCompPorvMultiplier_.empty())
this->rockCompPorvMultiplier_[globalDofIdx]
= problem.template rockCompPoroMultiplier<Scalar>(intQuants, globalDofIdx);
if (!this->rockCompTransMultiplier_.empty())
this->rockCompTransMultiplier_[globalDofIdx]
= problem.template rockCompTransMultiplier<Scalar>(intQuants, globalDofIdx);
const auto& matLawManager = problem.materialLawManager();
if (matLawManager->enableHysteresis()) {
if (!this->pcSwMdcOw_.empty() && !this->krnSwMdcOw_.empty()) {
matLawManager->oilWaterHysteresisParams(
this->pcSwMdcOw_[globalDofIdx], this->krnSwMdcOw_[globalDofIdx], globalDofIdx);
}
if (!this->pcSwMdcGo_.empty() && !this->krnSwMdcGo_.empty()) {
matLawManager->gasOilHysteresisParams(
this->pcSwMdcGo_[globalDofIdx], this->krnSwMdcGo_[globalDofIdx], globalDofIdx);
}
}
if (!this->ppcw_.empty()) {
this->ppcw_[globalDofIdx] = matLawManager->oilWaterScaledEpsInfoDrainage(globalDofIdx).maxPcow;
// printf("ppcw_[%d] = %lg\n", globalDofIdx, ppcw_[globalDofIdx]);
}
// hack to make the intial output of rs and rv Ecl compatible.
// For cells with swat == 1 Ecl outputs; rs = rsSat and rv=rvSat, in all but the initial step
// where it outputs rs and rv values calculated by the initialization. To be compatible we overwrite
// rs and rv with the values computed in the initially.
// Volume factors, densities and viscosities need to be recalculated with the updated rs and rv values.
// This can be removed when ebos has 100% controll over output
if ((elemCtx.simulator().episodeIndex() < 0) &&
FluidSystem::phaseIsActive(oilPhaseIdx) &&
FluidSystem::phaseIsActive(gasPhaseIdx))
{
const auto& fsInitial = problem.initialFluidState(globalDofIdx);
// use initial rs and rv values
if (!this->rv_.empty())
this->rv_[globalDofIdx] = fsInitial.Rv();
if (!this->rs_.empty())
this->rs_[globalDofIdx] = fsInitial.Rs();
if (!this->rsw_.empty())
this->rsw_[globalDofIdx] = fsInitial.Rsw();
if (!this->rvw_.empty())
this->rvw_[globalDofIdx] = fsInitial.Rvw();
// re-compute the volume factors, viscosities and densities if asked for
if (!this->density_[oilPhaseIdx].empty())
this->density_[oilPhaseIdx][globalDofIdx]
= FluidSystem::density(fsInitial, oilPhaseIdx, intQuants.pvtRegionIndex());
if (!this->density_[gasPhaseIdx].empty())
this->density_[gasPhaseIdx][globalDofIdx]
= FluidSystem::density(fsInitial, gasPhaseIdx, intQuants.pvtRegionIndex());
if (!this->invB_[oilPhaseIdx].empty())
this->invB_[oilPhaseIdx][globalDofIdx]
= FluidSystem::inverseFormationVolumeFactor(fsInitial, oilPhaseIdx, intQuants.pvtRegionIndex());
if (!this->invB_[gasPhaseIdx].empty())
this->invB_[gasPhaseIdx][globalDofIdx]
= FluidSystem::inverseFormationVolumeFactor(fsInitial, gasPhaseIdx, intQuants.pvtRegionIndex());
if (!this->viscosity_[oilPhaseIdx].empty())
this->viscosity_[oilPhaseIdx][globalDofIdx]
= FluidSystem::viscosity(fsInitial, oilPhaseIdx, intQuants.pvtRegionIndex());
if (!this->viscosity_[gasPhaseIdx].empty())
this->viscosity_[gasPhaseIdx][globalDofIdx]
= FluidSystem::viscosity(fsInitial, gasPhaseIdx, intQuants.pvtRegionIndex());
}
// Adding Well RFT data
const auto cartesianIdx = elemCtx.simulator().vanguard().cartesianIndex(globalDofIdx);
if (this->oilConnectionPressures_.count(cartesianIdx) > 0) {
this->oilConnectionPressures_[cartesianIdx] = getValue(fs.pressure(oilPhaseIdx));
}
if (this->waterConnectionSaturations_.count(cartesianIdx) > 0) {
this->waterConnectionSaturations_[cartesianIdx] = getValue(fs.saturation(waterPhaseIdx));
}
if (this->gasConnectionSaturations_.count(cartesianIdx) > 0) {
this->gasConnectionSaturations_[cartesianIdx] = getValue(fs.saturation(gasPhaseIdx));
}
// tracers
const auto& tracerModel = simulator_.problem().tracerModel();
if (! this->tracerConcentrations_.empty()) {
for (int tracerIdx = 0; tracerIdx < tracerModel.numTracers(); ++tracerIdx) {
if (this->tracerConcentrations_[tracerIdx].empty()) {
continue;
}
this->tracerConcentrations_[tracerIdx][globalDofIdx] =
tracerModel.tracerConcentration(tracerIdx, globalDofIdx);
}
}
// output residual
for ( int phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx )
{
if (!this->residual_[phaseIdx].empty()) {
const unsigned activeCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::solventComponentIndex(phaseIdx));
this->residual_[phaseIdx][globalDofIdx] = ebosResid[globalDofIdx][activeCompIdx];
}
}
}
}
void processElementFlows(const ElementContext& elemCtx)
{
OPM_TIMEBLOCK_LOCAL(processElementBlockData);
if (!std::is_same_v<Discretization, EcfvDiscretization<TypeTag>>)
return;
const auto& problem = elemCtx.simulator().problem();
for (unsigned dofIdx = 0; dofIdx < elemCtx.numPrimaryDof(/*timeIdx=*/0); ++dofIdx) {
unsigned globalDofIdx = elemCtx.globalSpaceIndex(dofIdx, /*timeIdx=*/0);
if (!problem.model().linearizer().getFlowsInfo().empty()) {
const auto& flowsInf = problem.model().linearizer().getFlowsInfo();
auto flowsInfos = flowsInf[globalDofIdx];
for (auto& flowsInfo : flowsInfos) {
if (flowsInfo.faceId == 1) {
if (!this->flowsi_[gasCompIdx].empty()) {
this->flowsi_[gasCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(gasCompIdx)];
}
if (!this->flowsi_[oilCompIdx].empty()) {
this->flowsi_[oilCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(oilCompIdx)];
}
if (!this->flowsi_[waterCompIdx].empty()) {
this->flowsi_[waterCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(waterCompIdx)];
}
}
if (flowsInfo.faceId == 3) {
if (!this->flowsj_[gasCompIdx].empty()) {
this->flowsj_[gasCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(gasCompIdx)];
}
if (!this->flowsj_[oilCompIdx].empty()) {
this->flowsj_[oilCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(oilCompIdx)];
}
if (!this->flowsj_[waterCompIdx].empty()) {
this->flowsj_[waterCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(waterCompIdx)];
}
}
if (flowsInfo.faceId == 5) {
if (!this->flowsk_[gasCompIdx].empty()) {
this->flowsk_[gasCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(gasCompIdx)];
}
if (!this->flowsk_[oilCompIdx].empty()) {
this->flowsk_[oilCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(oilCompIdx)];
}
if (!this->flowsk_[waterCompIdx].empty()) {
this->flowsk_[waterCompIdx][globalDofIdx]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(waterCompIdx)];
}
}
if (flowsInfo.faceId == -2) {
if (!this->flowsn_[gasCompIdx].second.first.empty()) {
this->flowsn_[gasCompIdx].second.first[flowsInfo.nncId] = flowsInfo.nncId;
this->flowsn_[gasCompIdx].second.second[flowsInfo.nncId]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(gasCompIdx)];
}
if (!this->flowsn_[oilCompIdx].second.first.empty()) {
this->flowsn_[oilCompIdx].second.first[flowsInfo.nncId] = flowsInfo.nncId;
this->flowsn_[oilCompIdx].second.second[flowsInfo.nncId]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(oilCompIdx)];
}
if (!this->flowsn_[waterCompIdx].second.first.empty()) {
this->flowsn_[waterCompIdx].second.first[flowsInfo.nncId] = flowsInfo.nncId;
this->flowsn_[waterCompIdx].second.second[flowsInfo.nncId]
= flowsInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(waterCompIdx)];
}
}
}
}
// flores
if (!problem.model().linearizer().getFloresInfo().empty()) {
const auto& floresInf = problem.model().linearizer().getFloresInfo();
auto floresInfos =floresInf[globalDofIdx];
for (auto& floresInfo : floresInfos) {
if (floresInfo.faceId == 1) {
if (!this->floresi_[gasCompIdx].empty()) {
this->floresi_[gasCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(gasCompIdx)];
}
if (!this->floresi_[oilCompIdx].empty()) {
this->floresi_[oilCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(oilCompIdx)];
}
if (!this->floresi_[waterCompIdx].empty()) {
this->floresi_[waterCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(waterCompIdx)];
}
}
if (floresInfo.faceId == 3) {
if (!this->floresj_[gasCompIdx].empty()) {
this->floresj_[gasCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(gasCompIdx)];
}
if (!this->floresj_[oilCompIdx].empty()) {
this->floresj_[oilCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(oilCompIdx)];
}
if (!this->floresj_[waterCompIdx].empty()) {
this->floresj_[waterCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(waterCompIdx)];
}
}
if (floresInfo.faceId == 5) {
if (!this->floresk_[gasCompIdx].empty()) {
this->floresk_[gasCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(gasCompIdx)];
}
if (!this->floresk_[oilCompIdx].empty()) {
this->floresk_[oilCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(oilCompIdx)];
}
if (!this->floresk_[waterCompIdx].empty()) {
this->floresk_[waterCompIdx][globalDofIdx]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(waterCompIdx)];
}
}
if (floresInfo.faceId == -2) {
if (!this->floresn_[gasCompIdx].second.first.empty()) {
this->floresn_[gasCompIdx].second.first[floresInfo.nncId] = floresInfo.nncId;
this->floresn_[gasCompIdx].second.second[floresInfo.nncId]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(gasCompIdx)];
}
if (!this->floresn_[oilCompIdx].second.first.empty()) {
this->floresn_[oilCompIdx].second.first[floresInfo.nncId] = floresInfo.nncId;
this->floresn_[oilCompIdx].second.second[floresInfo.nncId]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(oilCompIdx)];
}
if (!this->floresn_[waterCompIdx].second.first.empty()) {
this->floresn_[waterCompIdx].second.first[floresInfo.nncId] = floresInfo.nncId;
this->floresn_[waterCompIdx].second.second[floresInfo.nncId]
= floresInfo.flow[conti0EqIdx + Indices::canonicalToActiveComponentIndex(waterCompIdx)];
}
}
}
}
}
}
void processElementBlockData(const ElementContext& elemCtx)
{
OPM_TIMEBLOCK_LOCAL(processElementBlockData);
if (!std::is_same<Discretization, EcfvDiscretization<TypeTag>>::value)
return;
const auto& problem = elemCtx.simulator().problem();
for (unsigned dofIdx = 0; dofIdx < elemCtx.numPrimaryDof(/*timeIdx=*/0); ++dofIdx) {
// Adding block data
const auto globalDofIdx = elemCtx.globalSpaceIndex(dofIdx, /*timeIdx=*/0);
const auto cartesianIdx = elemCtx.simulator().vanguard().cartesianIndex(globalDofIdx);
const auto& intQuants = elemCtx.intensiveQuantities(dofIdx, /*timeIdx=*/0);
const auto& fs = intQuants.fluidState();
for (auto& val : this->blockData_) {
const auto& key = val.first;
assert(key.second > 0);
unsigned int cartesianIdxBlock = key.second - 1;
if (cartesianIdx == cartesianIdxBlock) {
if ((key.first == "BWSAT") || (key.first == "BSWAT"))
val.second = getValue(fs.saturation(waterPhaseIdx));
else if ((key.first == "BGSAT") || (key.first == "BSGAS"))
val.second = getValue(fs.saturation(gasPhaseIdx));
else if ((key.first == "BOSAT") || (key.first == "BSOIL"))
val.second = getValue(fs.saturation(oilPhaseIdx));
else if (key.first == "BNSAT")
val.second = intQuants.solventSaturation().value();
else if ((key.first == "BPR") || (key.first == "BPRESSUR")) {
if (FluidSystem::phaseIsActive(oilPhaseIdx))
val.second = getValue(fs.pressure(oilPhaseIdx));
else if (FluidSystem::phaseIsActive(gasPhaseIdx))
val.second = getValue(fs.pressure(gasPhaseIdx));
else if (FluidSystem::phaseIsActive(waterPhaseIdx))
val.second = getValue(fs.pressure(waterPhaseIdx));
}
else if ((key.first == "BTCNFHEA") || (key.first == "BTEMP")) {
if (FluidSystem::phaseIsActive(oilPhaseIdx))
val.second = getValue(fs.temperature(oilPhaseIdx));
else if (FluidSystem::phaseIsActive(gasPhaseIdx))
val.second = getValue(fs.temperature(gasPhaseIdx));
else if (FluidSystem::phaseIsActive(waterPhaseIdx))
val.second = getValue(fs.temperature(waterPhaseIdx));
}
else if (key.first == "BWKR" || key.first == "BKRW")
val.second = getValue(intQuants.relativePermeability(waterPhaseIdx));
else if (key.first == "BGKR" || key.first == "BKRG")
val.second = getValue(intQuants.relativePermeability(gasPhaseIdx));
else if (key.first == "BOKR" || key.first == "BKRO")
val.second = getValue(intQuants.relativePermeability(oilPhaseIdx));
else if (key.first == "BKROG") {
const auto& materialParams = problem.materialLawParams(elemCtx, dofIdx, /* timeIdx = */ 0);
const auto krog
= MaterialLaw::template relpermOilInOilGasSystem<Evaluation>(materialParams, fs);
val.second = getValue(krog);
}
else if (key.first == "BKROW") {
const auto& materialParams = problem.materialLawParams(elemCtx, dofIdx, /* timeIdx = */ 0);
const auto krow
= MaterialLaw::template relpermOilInOilWaterSystem<Evaluation>(materialParams, fs);
val.second = getValue(krow);
}
else if (key.first == "BWPC")
val.second = getValue(fs.pressure(oilPhaseIdx)) - getValue(fs.pressure(waterPhaseIdx));
else if (key.first == "BGPC")
val.second = getValue(fs.pressure(gasPhaseIdx)) - getValue(fs.pressure(oilPhaseIdx));
else if (key.first == "BWPR")
val.second = getValue(fs.pressure(waterPhaseIdx));
else if (key.first == "BGPR")
val.second = getValue(fs.pressure(gasPhaseIdx));
else if (key.first == "BVWAT" || key.first == "BWVIS")
val.second = getValue(fs.viscosity(waterPhaseIdx));
else if (key.first == "BVGAS" || key.first == "BGVIS")
val.second = getValue(fs.viscosity(gasPhaseIdx));
else if (key.first == "BVOIL" || key.first == "BOVIS")
val.second = getValue(fs.viscosity(oilPhaseIdx));
else if ((key.first == "BODEN") || (key.first == "BDENO"))
val.second = getValue(fs.density(oilPhaseIdx));
else if ((key.first == "BGDEN") || (key.first == "BDENG"))
val.second = getValue(fs.density(gasPhaseIdx));
else if ((key.first == "BWDEN") || (key.first == "BDENW"))
val.second = getValue(fs.density(waterPhaseIdx));
else if ((key.first == "BRPV") ||
(key.first == "BOPV") ||
(key.first == "BWPV") ||
(key.first == "BGPV"))
{
if (key.first == "BRPV") {
val.second = 1.0;
}
else if (key.first == "BOPV") {
val.second = getValue(fs.saturation(oilPhaseIdx));
}
else if (key.first == "BWPV") {
val.second = getValue(fs.saturation(waterPhaseIdx));
}
else {
val.second = getValue(fs.saturation(gasPhaseIdx));
}
// Include active pore-volume.
val.second *= elemCtx.simulator().model().dofTotalVolume(globalDofIdx)
* getValue(intQuants.porosity());
}
else if (key.first == "BRS")
val.second = getValue(fs.Rs());
else if (key.first == "BRV")
val.second = getValue(fs.Rv());
else if ((key.first == "BOIP") || (key.first == "BOIPL") || (key.first == "BOIPG") ||
(key.first == "BGIP") || (key.first == "BGIPL") || (key.first == "BGIPG") ||
(key.first == "BWIP"))
{
if ((key.first == "BOIP") || (key.first == "BOIPL")) {
val.second = getValue(fs.invB(oilPhaseIdx)) * getValue(fs.saturation(oilPhaseIdx));
if (key.first == "BOIP") {
val.second += getValue(fs.Rv()) * getValue(fs.invB(gasPhaseIdx))
* getValue(fs.saturation(gasPhaseIdx));
}
}
else if (key.first == "BOIPG") {
val.second = getValue(fs.Rv()) * getValue(fs.invB(gasPhaseIdx))
* getValue(fs.saturation(gasPhaseIdx));
}
else if ((key.first == "BGIP") || (key.first == "BGIPG")) {
val.second = getValue(fs.invB(gasPhaseIdx)) * getValue(fs.saturation(gasPhaseIdx));
if (key.first == "BGIP") {
val.second += getValue(fs.Rs()) * getValue(fs.invB(oilPhaseIdx))
* getValue(fs.saturation(oilPhaseIdx));
}
}
else if (key.first == "BGIPL") {
val.second = getValue(fs.Rs()) * getValue(fs.invB(oilPhaseIdx))
* getValue(fs.saturation(oilPhaseIdx));
}
else { // BWIP
val.second = getValue(fs.invB(waterPhaseIdx)) * getValue(fs.saturation(waterPhaseIdx));
}
// Include active pore-volume.
val.second *= elemCtx.simulator().model().dofTotalVolume(globalDofIdx)
* getValue(intQuants.porosity());
}
else if (key.first == "BFLOWI")
val.second = this->flowsi_[waterCompIdx][globalDofIdx];
else if (key.first == "BFLOWJ")
val.second = this->flowsj_[waterCompIdx][globalDofIdx];
else if (key.first == "BFLOWK")
val.second = this->flowsk_[waterCompIdx][globalDofIdx];
else {
std::string logstring = "Keyword '";
logstring.append(key.first);
logstring.append("' is unhandled for output to file.");
OpmLog::warning("Unhandled output keyword", logstring);
}
}
}
}
}
/*!
* \brief Capture connection fluxes, particularly to account for inter-region flows.
*
* \tparam ActiveIndex Callable type, typically a lambda, that enables
* retrieving the active index, on the local MPI rank, of a
* particular cell/element. Must support a function call operator of
* the form
\code
int operator()(const Element& elem) const
\endcode
*
* \tparam CartesianIndex Callable type, typically a lambda, that
* enables retrieving the globally unique Cartesian index of a
* particular cell/element given its active index on the local MPI
* rank. Must support a function call operator of the form
\code
int operator()(const int activeIndex) const
\endcode
*
* \param[in] elemCtx Primary lookup structure for per-cell/element
* dynamic information.
*
* \param[in] activeIndex Mapping from cell/elements to linear indices
* on local MPI rank.
*
* \param[in] cartesianIndex Mapping from active index on local MPI rank
* to globally unique Cartesian cell/element index.
*/
template <class ActiveIndex, class CartesianIndex>
void processFluxes(const ElementContext& elemCtx,
ActiveIndex&& activeIndex,
CartesianIndex&& cartesianIndex)
{
OPM_TIMEBLOCK_LOCAL(processFluxes);
const auto identifyCell = [&activeIndex, &cartesianIndex](const Element& elem)
-> EclInterRegFlowMap::Cell
{
const auto cellIndex = activeIndex(elem);
return {
static_cast<int>(cellIndex),
cartesianIndex(cellIndex),
elem.partitionType() == Dune::InteriorEntity
};
};
const auto timeIdx = 0u;
const auto& stencil = elemCtx.stencil(timeIdx);
const auto numInteriorFaces = elemCtx.numInteriorFaces(timeIdx);
for (auto scvfIdx = 0 * numInteriorFaces; scvfIdx < numInteriorFaces; ++scvfIdx) {
const auto& face = stencil.interiorFace(scvfIdx);
const auto left = identifyCell(stencil.element(face.interiorIndex()));
const auto right = identifyCell(stencil.element(face.exteriorIndex()));
const auto rates = this->
getComponentSurfaceRates(elemCtx, face.area(), scvfIdx, timeIdx);
this->interRegionFlows_.addConnection(left, right, rates);
}
}
/*!
* \brief Prepare for capturing connection fluxes, particularly to
* account for inter-region flows.
*/
void initializeFluxData()
{
// Inter-region flow rates. Note: ".clear()" prepares to accumulate
// contributions per bulk connection between FIP regions.
this->interRegionFlows_.clear();
}
/*!
* \brief Finalize capturing connection fluxes.
*/
void finalizeFluxData()
{
this->interRegionFlows_.compress();
}
/*!
* \brief Get read-only access to collection of inter-region flows.
*/
const EclInterRegFlowMap& getInterRegFlows() const
{
return this->interRegionFlows_;
}
template <class FluidState>
void assignToFluidState(FluidState& fs, unsigned elemIdx) const
{
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
if (this->saturation_[phaseIdx].empty())
continue;
fs.setSaturation(phaseIdx, this->saturation_[phaseIdx][elemIdx]);
}
if (!this->fluidPressure_.empty()) {
// this assumes that capillary pressures only depend on the phase saturations
// and possibly on temperature. (this is always the case for ECL problems.)
std::array<Scalar, numPhases> pc = {0};
const MaterialLawParams& matParams = simulator_.problem().materialLawParams(elemIdx);
MaterialLaw::capillaryPressures(pc, matParams, fs);
Valgrind::CheckDefined(this->fluidPressure_[elemIdx]);
Valgrind::CheckDefined(pc);
assert(FluidSystem::phaseIsActive(oilPhaseIdx));
for (unsigned phaseIdx = 0; phaseIdx < numPhases; ++phaseIdx) {
if (!FluidSystem::phaseIsActive(phaseIdx))
continue;
fs.setPressure(phaseIdx, this->fluidPressure_[elemIdx] + (pc[phaseIdx] - pc[oilPhaseIdx]));
}
}
if (!this->temperature_.empty())
fs.setTemperature(this->temperature_[elemIdx]);
if (!this->rs_.empty())
fs.setRs(this->rs_[elemIdx]);
if (!this->rsw_.empty())
fs.setRsw(this->rsw_[elemIdx]);
if (!this->rv_.empty())
fs.setRv(this->rv_[elemIdx]);
if (!this->rvw_.empty())
fs.setRvw(this->rvw_[elemIdx]);
}
void initHysteresisParams(Simulator& simulator, unsigned elemIdx) const
{
if (!this->soMax_.empty())
simulator.problem().setMaxOilSaturation(elemIdx, this->soMax_[elemIdx]);
if (simulator.problem().materialLawManager()->enableHysteresis()) {
auto matLawManager = simulator.problem().materialLawManager();
if (!this->pcSwMdcOw_.empty() && !this->krnSwMdcOw_.empty()) {
matLawManager->setOilWaterHysteresisParams(
this->pcSwMdcOw_[elemIdx], this->krnSwMdcOw_[elemIdx], elemIdx);
}
if (!this->pcSwMdcGo_.empty() && !this->krnSwMdcGo_.empty()) {
matLawManager->setGasOilHysteresisParams(
this->pcSwMdcGo_[elemIdx], this->krnSwMdcGo_[elemIdx], elemIdx);
}
}
if (simulator_.vanguard().eclState().fieldProps().has_double("SWATINIT")) {
simulator.problem().materialLawManager()
->applyRestartSwatInit(elemIdx, this->ppcw_[elemIdx]);
}
}
void updateFluidInPlace(const ElementContext& elemCtx)
{
for (unsigned dofIdx = 0; dofIdx < elemCtx.numPrimaryDof(/*timeIdx=*/0); ++dofIdx) {
updateFluidInPlace_(elemCtx, dofIdx);
}
}
void updateFluidInPlace(const unsigned globalDofIdx,
const IntensiveQuantities& intQuants,
const double totVolume)
{
this->updateFluidInPlace_(globalDofIdx, intQuants, totVolume);
}
private:
bool isDefunctParallelWell(std::string wname) const override
{
if (simulator_.gridView().comm().size() == 1)
return false;
const auto& parallelWells = simulator_.vanguard().parallelWells();
std::pair<std::string, bool> value {wname, true};
auto candidate = std::lower_bound(parallelWells.begin(), parallelWells.end(), value);
return candidate == parallelWells.end() || *candidate != value;
}
void updateFluidInPlace_(const ElementContext& elemCtx, const unsigned dofIdx)
{
const auto& intQuants = elemCtx.intensiveQuantities(dofIdx, /*timeIdx=*/0);
const unsigned globalDofIdx = elemCtx.globalSpaceIndex(dofIdx, /*timeIdx=*/0);
const auto totVolume = elemCtx.simulator().model().dofTotalVolume(globalDofIdx);
this->updateFluidInPlace_(globalDofIdx, intQuants, totVolume);
}
void updateFluidInPlace_(const unsigned globalDofIdx,
const IntensiveQuantities& intQuants,
const double totVolume)
{
OPM_TIMEBLOCK_LOCAL(updateFluidInPlace);
this->updateTotalVolumesAndPressures_(globalDofIdx, intQuants, totVolume);
if (this->computeFip_) {
this->updatePhaseInplaceVolumes_(globalDofIdx, intQuants, totVolume);
}
}
void createLocalRegion_(std::vector<int>& region)
{
std::size_t elemIdx = 0;
for (const auto& elem : elements(simulator_.gridView())) {
if (elem.partitionType() != Dune::InteriorEntity)
region[elemIdx] = 0;
++elemIdx;
}
}
/*!
* \brief Compute surface level component flow rates across a single
* intersection.
*
* \param[in] elemCtx Primary lookup structure for per-cell/element
* dynamic information.
*
* \param[in] scvfIdx Linear index of current interior bulk connection.
*
* \param[in] timeIdx Historical time-point at which to evaluate dynamic
* quantities (e.g., reciprocal FVF or dissolved gas concentration).
* Zero for the current time.
*
* \return Surface level component flow rates.
*/
data::InterRegFlowMap::FlowRates
getComponentSurfaceRates(const ElementContext& elemCtx,
const Scalar faceArea,
const std::size_t scvfIdx,
const std::size_t timeIdx) const
{
using Component = data::InterRegFlowMap::Component;
auto rates = data::InterRegFlowMap::FlowRates {};
const auto& extQuant = elemCtx.extensiveQuantities(scvfIdx, timeIdx);
const auto alpha = getValue(extQuant.extrusionFactor()) * faceArea;
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
const auto& up = elemCtx
.intensiveQuantities(extQuant.upstreamIndex(oilPhaseIdx), timeIdx);
using FluidState = std::remove_cv_t<std::remove_reference_t<
decltype(up.fluidState())>>;
const auto pvtReg = up.pvtRegionIndex();
const auto bO = getValue(getInvB_<FluidSystem, FluidState, Scalar>
(up.fluidState(), oilPhaseIdx, pvtReg));
const auto qO = alpha * bO * getValue(extQuant.volumeFlux(oilPhaseIdx));
rates[Component::Oil] += qO;
if (FluidSystem::phaseIsActive(gasPhaseIdx)) {
const auto Rs = getValue(
BlackOil::getRs_<FluidSystem, FluidState, Scalar>
(up.fluidState(), pvtReg));
rates[Component::Gas] += qO * Rs;
rates[Component::Disgas] += qO * Rs;
}
}
if (FluidSystem::phaseIsActive(gasPhaseIdx)) {
const auto& up = elemCtx
.intensiveQuantities(extQuant.upstreamIndex(gasPhaseIdx), timeIdx);
using FluidState = std::remove_cv_t<std::remove_reference_t<
decltype(up.fluidState())>>;
const auto pvtReg = up.pvtRegionIndex();
const auto bG = getValue(getInvB_<FluidSystem, FluidState, Scalar>
(up.fluidState(), gasPhaseIdx, pvtReg));
const auto qG = alpha * bG * getValue(extQuant.volumeFlux(gasPhaseIdx));
rates[Component::Gas] += qG;
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
const auto Rv = getValue(
BlackOil::getRv_<FluidSystem, FluidState, Scalar>
(up.fluidState(), pvtReg));
rates[Component::Oil] += qG * Rv;
rates[Component::Vapoil] += qG * Rv;
}
}
if (FluidSystem::phaseIsActive(waterPhaseIdx)) {
const auto& up = elemCtx
.intensiveQuantities(extQuant.upstreamIndex(waterPhaseIdx), timeIdx);
using FluidState = std::remove_cv_t<std::remove_reference_t<
decltype(up.fluidState())>>;
const auto pvtReg = up.pvtRegionIndex();
const auto bW = getValue(getInvB_<FluidSystem, FluidState, Scalar>
(up.fluidState(), waterPhaseIdx, pvtReg));
rates[Component::Water] +=
alpha * bW * getValue(extQuant.volumeFlux(waterPhaseIdx));
}
return rates;
}
template <typename FluidState>
Scalar hydroCarbonFraction(const FluidState& fs) const
{
if (this->eclState_.runspec().co2Storage()) {
// CO2 storage: Hydrocarbon volume is full pore-volume.
return 1.0;
}
// Common case. Hydrocarbon volume is fraction occupied by actual
// hydrocarbons.
auto hydrocarbon = Scalar {0};
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
hydrocarbon += getValue(fs.saturation(oilPhaseIdx));
}
if (FluidSystem::phaseIsActive(gasPhaseIdx)) {
hydrocarbon += getValue(fs.saturation(gasPhaseIdx));
}
return hydrocarbon;
}
void updateTotalVolumesAndPressures_(const unsigned globalDofIdx,
const IntensiveQuantities& intQuants,
const double totVolume)
{
const auto& fs = intQuants.fluidState();
const double pv = totVolume * intQuants.porosity().value();
const auto hydrocarbon = this->hydroCarbonFraction(fs);
if (! this->hydrocarbonPoreVolume_.empty()) {
this->fip_[Inplace::Phase::PoreVolume][globalDofIdx] =
totVolume * intQuants.referencePorosity();
this->dynamicPoreVolume_[globalDofIdx] = pv;
this->hydrocarbonPoreVolume_[globalDofIdx] = pv * hydrocarbon;
}
if (!this->pressureTimesHydrocarbonVolume_.empty() &&
!this->pressureTimesPoreVolume_.empty())
{
assert(this->hydrocarbonPoreVolume_.size() == this->pressureTimesHydrocarbonVolume_.size());
assert(this->fip_[Inplace::Phase::PoreVolume].size() == this->pressureTimesPoreVolume_.size());
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
this->pressureTimesPoreVolume_[globalDofIdx] =
getValue(fs.pressure(oilPhaseIdx)) * pv;
this->pressureTimesHydrocarbonVolume_[globalDofIdx] =
this->pressureTimesPoreVolume_[globalDofIdx] * hydrocarbon;
}
else if (FluidSystem::phaseIsActive(gasPhaseIdx)) {
this->pressureTimesPoreVolume_[globalDofIdx] =
getValue(fs.pressure(gasPhaseIdx)) * pv;
this->pressureTimesHydrocarbonVolume_[globalDofIdx] =
this->pressureTimesPoreVolume_[globalDofIdx] * hydrocarbon;
}
else if (FluidSystem::phaseIsActive(waterPhaseIdx)) {
this->pressureTimesPoreVolume_[globalDofIdx] =
getValue(fs.pressure(waterPhaseIdx)) * pv;
}
}
}
void updatePhaseInplaceVolumes_(const unsigned globalDofIdx,
const IntensiveQuantities& intQuants,
const double totVolume)
{
std::array<Scalar, FluidSystem::numPhases> fip {};
std::array<Scalar, FluidSystem::numPhases> fipr{}; // at reservoir condition
const auto& fs = intQuants.fluidState();
const auto pv = totVolume * intQuants.porosity().value();
for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++phaseIdx) {
if (!FluidSystem::phaseIsActive(phaseIdx)) {
continue;
}
const auto b = getValue(fs.invB(phaseIdx));
const auto s = getValue(fs.saturation(phaseIdx));
fipr[phaseIdx] = s * pv;
fip [phaseIdx] = b * fipr[phaseIdx];
}
this->updateInplaceVolumesSurface(globalDofIdx, fip);
this->updateInplaceVolumesReservoir(globalDofIdx, fs, fipr);
if (FluidSystem::phaseIsActive(oilPhaseIdx) &&
FluidSystem::phaseIsActive(gasPhaseIdx))
{
this->updateOilGasDistribution(globalDofIdx, fs, fip);
}
if (FluidSystem::phaseIsActive(waterPhaseIdx) &&
FluidSystem::phaseIsActive(gasPhaseIdx))
{
this->updateGasWaterDistribution(globalDofIdx, fs, fip);
}
if (FluidSystem::phaseIsActive(gasPhaseIdx) &&
(!this->fip_[Inplace::Phase::CO2InGasPhaseInMob].empty() ||
!this->fip_[Inplace::Phase::CO2InGasPhaseMob].empty()))
{
this->updateCO2InGas(globalDofIdx, pv, fs);
}
if (!this->fip_[Inplace::Phase::CO2InWaterPhase].empty() &&
(FluidSystem::phaseIsActive(waterPhaseIdx) ||
FluidSystem::phaseIsActive(oilPhaseIdx)))
{
const auto co2InWater = FluidSystem::phaseIsActive(oilPhaseIdx)
? this->co2InWaterFromOil(fs, pv)
: this->co2InWaterFromWater(fs, pv);
this->fip_[Inplace::Phase::CO2InWaterPhase][globalDofIdx] = co2InWater;
}
}
template <typename FIPArray>
void updateInplaceVolumesSurface(const unsigned globalDofIdx,
const FIPArray& fip)
{
if (FluidSystem::phaseIsActive(oilPhaseIdx) &&
!this->fip_[Inplace::Phase::OIL].empty())
{
this->fip_[Inplace::Phase::OIL][globalDofIdx] = fip[oilPhaseIdx];
}
if (FluidSystem::phaseIsActive(oilPhaseIdx) &&
!this->fip_[Inplace::Phase::OilInLiquidPhase].empty())
{
this->fip_[Inplace::Phase::OilInLiquidPhase][globalDofIdx] = fip[oilPhaseIdx];
}
if (FluidSystem::phaseIsActive(gasPhaseIdx) &&
!this->fip_[Inplace::Phase::GAS].empty())
{
this->fip_[Inplace::Phase::GAS][globalDofIdx] = fip[gasPhaseIdx];
}
if (FluidSystem::phaseIsActive(gasPhaseIdx) &&
!this->fip_[Inplace::Phase::GasInGasPhase].empty())
{
this->fip_[Inplace::Phase::GasInGasPhase][globalDofIdx] = fip[gasPhaseIdx];
}
if (FluidSystem::phaseIsActive(waterPhaseIdx) &&
!this->fip_[Inplace::Phase::WATER].empty())
{
this->fip_[Inplace::Phase::WATER][globalDofIdx] = fip[waterPhaseIdx];
}
}
template <typename FluidState, typename FIPArray>
void updateInplaceVolumesReservoir(const unsigned globalDofIdx,
const FluidState& fs,
const FIPArray& fipr)
{
if (FluidSystem::phaseIsActive(oilPhaseIdx) &&
!this->fip_[Inplace::Phase::OilResVolume].empty())
{
this->fip_[Inplace::Phase::OilResVolume][globalDofIdx] = fipr[oilPhaseIdx];
}
if (FluidSystem::phaseIsActive(gasPhaseIdx) &&
!this->fip_[Inplace::Phase::GasResVolume].empty())
{
this->fip_[Inplace::Phase::GasResVolume][globalDofIdx] = fipr[gasPhaseIdx];
}
if (FluidSystem::phaseIsActive(waterPhaseIdx) &&
!this->fip_[Inplace::Phase::WaterResVolume].empty())
{
this->fip_[Inplace::Phase::WaterResVolume][globalDofIdx] = fipr[waterPhaseIdx];
}
if (FluidSystem::phaseIsActive(waterPhaseIdx) &&
!this->fip_[Inplace::Phase::SALT].empty())
{
this->fip_[Inplace::Phase::SALT][globalDofIdx] =
fipr[waterPhaseIdx] * fs.saltConcentration().value();
}
}
template <typename FluidState, typename FIPArray>
void updateOilGasDistribution(const unsigned globalDofIdx,
const FluidState& fs,
const FIPArray& fip)
{
// Gas dissolved in oil and vaporized oil
const auto gasInPlaceLiquid = getValue(fs.Rs()) * fip[oilPhaseIdx];
const auto oilInPlaceGas = getValue(fs.Rv()) * fip[gasPhaseIdx];
if (!this->fip_[Inplace::Phase::GasInLiquidPhase].empty()) {
this->fip_[Inplace::Phase::GasInLiquidPhase][globalDofIdx] = gasInPlaceLiquid;
}
if (!this->fip_[Inplace::Phase::OilInGasPhase].empty()) {
this->fip_[Inplace::Phase::OilInGasPhase][globalDofIdx] = oilInPlaceGas;
}
// Add dissolved gas and vaporized oil to total Fip
if (!this->fip_[Inplace::Phase::OIL].empty()) {
this->fip_[Inplace::Phase::OIL][globalDofIdx] += oilInPlaceGas;
}
if (!this->fip_[Inplace::Phase::GAS].empty()) {
this->fip_[Inplace::Phase::GAS][globalDofIdx] += gasInPlaceLiquid;
}
}
template <typename FluidState, typename FIPArray>
void updateGasWaterDistribution(const unsigned globalDofIdx,
const FluidState& fs,
const FIPArray& fip)
{
// Gas dissolved in water and vaporized water
const auto gasInPlaceWater = getValue(fs.Rsw()) * fip[waterPhaseIdx];
const auto waterInPlaceGas = getValue(fs.Rvw()) * fip[gasPhaseIdx];
if (!this->fip_[Inplace::Phase::WaterInGasPhase].empty()) {
this->fip_[Inplace::Phase::WaterInGasPhase][globalDofIdx] = waterInPlaceGas;
}
if (!this->fip_[Inplace::Phase::WaterInWaterPhase].empty()) {
this->fip_[Inplace::Phase::WaterInWaterPhase][globalDofIdx] = fip[waterPhaseIdx];
}
// For water+gas cases the gas in water is added to the GIPL value
if (!this->fip_[Inplace::Phase::GasInLiquidPhase].empty() &&
!FluidSystem::phaseIsActive(oilPhaseIdx))
{
this->fip_[Inplace::Phase::GasInLiquidPhase][globalDofIdx] = gasInPlaceWater;
}
// Add dissolved gas and vaporized water to total Fip
if (!this->fip_[Inplace::Phase::WATER].empty()) {
this->fip_[Inplace::Phase::WATER][globalDofIdx] += waterInPlaceGas;
}
if (!this->fip_[Inplace::Phase::GAS].empty()) {
this->fip_[Inplace::Phase::GAS][globalDofIdx] += gasInPlaceWater;
}
}
template <typename FluidState>
void updateCO2InGas(const unsigned globalDofIdx,
const double pv,
const FluidState& fs)
{
const auto& scaledDrainageInfo = this->simulator_.problem().materialLawManager()
->oilWaterScaledEpsInfoDrainage(globalDofIdx);
Scalar sgcr = scaledDrainageInfo.Sgcr;
if (this->simulator_.problem().materialLawManager()->enableHysteresis()) {
const auto& matParams = simulator_.problem().materialLawParams(globalDofIdx);
sgcr = MaterialLaw::trappedGasSaturation(matParams);
}
const double sg = getValue(fs.saturation(gasPhaseIdx));
const double rhog = getValue(fs.density(gasPhaseIdx));
const double xgW = FluidSystem::phaseIsActive(waterPhaseIdx)
? FluidSystem::convertRvwToXgW(getValue(fs.Rvw()), fs.pvtRegionIndex())
: FluidSystem::convertRvToXgO(getValue(fs.Rv()), fs.pvtRegionIndex());
const Scalar mM = FluidSystem::molarMass(gasCompIdx, fs.pvtRegionIndex());
if (!this->fip_[Inplace::Phase::CO2InGasPhaseInMob].empty()) {
const Scalar imMobileGas = (1 - xgW) * pv * rhog / mM * std::min(sgcr , sg);
this->fip_[Inplace::Phase::CO2InGasPhaseInMob][globalDofIdx] = imMobileGas;
}
if (!this->fip_[Inplace::Phase::CO2InGasPhaseMob].empty()) {
const Scalar mobileGas = (1 - xgW) * pv * rhog / mM * std::max(0.0, sg - sgcr);
this->fip_[Inplace::Phase::CO2InGasPhaseMob][globalDofIdx] = mobileGas;
}
}
template <typename FluidState>
Scalar co2InWaterFromWater(const FluidState& fs, const double pv) const
{
const double rhow = getValue(fs.density(waterPhaseIdx));
const double sw = getValue(fs.saturation(waterPhaseIdx));
const double xwG = FluidSystem::convertRswToXwG(getValue(fs.Rsw()), fs.pvtRegionIndex());
const Scalar mM = FluidSystem::molarMass(gasCompIdx, fs.pvtRegionIndex());
return xwG * pv * rhow * sw / mM;
}
template <typename FluidState>
Scalar co2InWaterFromOil(const FluidState& fs, const double pv) const
{
const double rhoo = getValue(fs.density(oilPhaseIdx));
const double so = getValue(fs.saturation(oilPhaseIdx));
const double xoG = FluidSystem::convertRsToXoG(getValue(fs.Rs()), fs.pvtRegionIndex());
const Scalar mM = FluidSystem::molarMass(gasCompIdx, fs.pvtRegionIndex());
return xoG * pv * rhoo * so / mM;
}
const Simulator& simulator_;
};
} // namespace Opm
#endif
Reference in New Issue View Git Blame Copy Permalink