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opm-simulators/opm/simulators/flow/TracerModel.hpp
Svenn Tveit 87362d5037 Accumulate segment rates and minor fixes
2024-06-12 14:18:32 +02:00

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// -*- 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::TracerModel
*/
#ifndef OPM_TRACER_MODEL_HPP
#define OPM_TRACER_MODEL_HPP
#include <opm/common/OpmLog/OpmLog.hpp>
#include <opm/models/utils/propertysystem.hh>
#include <opm/simulators/flow/GenericTracerModel.hpp>
#include <opm/simulators/utils/VectorVectorDataHandle.hpp>
#include <array>
#include <cstddef>
#include <memory>
#include <stdexcept>
#include <string>
#include <vector>
namespace Opm::Properties {
template<class TypeTag, class MyTypeTag>
struct EnableTracerModel {
using type = UndefinedProperty;
};
} // namespace Opm::Properties
namespace Opm {
/*!
* \ingroup BlackOilSimulator
*
* \brief A class which handles tracers as specified in by ECL
*/
template <class TypeTag>
class TracerModel : public GenericTracerModel<GetPropType<TypeTag, Properties::Grid>,
GetPropType<TypeTag, Properties::GridView>,
GetPropType<TypeTag, Properties::DofMapper>,
GetPropType<TypeTag, Properties::Stencil>,
GetPropType<TypeTag, Properties::FluidSystem>,
GetPropType<TypeTag, Properties::Scalar>>
{
using BaseType = GenericTracerModel<GetPropType<TypeTag, Properties::Grid>,
GetPropType<TypeTag, Properties::GridView>,
GetPropType<TypeTag, Properties::DofMapper>,
GetPropType<TypeTag, Properties::Stencil>,
GetPropType<TypeTag, Properties::FluidSystem>,
GetPropType<TypeTag, Properties::Scalar>>;
using Simulator = GetPropType<TypeTag, Properties::Simulator>;
using GridView = GetPropType<TypeTag, Properties::GridView>;
using Grid = GetPropType<TypeTag, Properties::Grid>;
using Scalar = GetPropType<TypeTag, Properties::Scalar>;
using Stencil = GetPropType<TypeTag, Properties::Stencil>;
using FluidSystem = GetPropType<TypeTag, Properties::FluidSystem>;
using ElementContext = GetPropType<TypeTag, Properties::ElementContext>;
using RateVector = GetPropType<TypeTag, Properties::RateVector>;
using Indices = GetPropType<TypeTag, Properties::Indices>;
using TracerEvaluation = DenseAd::Evaluation<Scalar,1>;
using TracerMatrix = typename BaseType::TracerMatrix;
using TracerVector = typename BaseType::TracerVector;
enum { numEq = getPropValue<TypeTag, Properties::NumEq>() };
enum { numPhases = FluidSystem::numPhases };
enum { waterPhaseIdx = FluidSystem::waterPhaseIdx };
enum { oilPhaseIdx = FluidSystem::oilPhaseIdx };
enum { gasPhaseIdx = FluidSystem::gasPhaseIdx };
public:
TracerModel(Simulator& simulator)
: BaseType(simulator.vanguard().gridView(),
simulator.vanguard().eclState(),
simulator.vanguard().cartesianIndexMapper(),
simulator.model().dofMapper(),
simulator.vanguard().cellCentroids())
, simulator_(simulator)
, tbatch({waterPhaseIdx, oilPhaseIdx, gasPhaseIdx})
, wat_(tbatch[0])
, oil_(tbatch[1])
, gas_(tbatch[2])
{ }
/*
The initialization of the tracer model is a three step process:
1. The init() method is called. This will allocate buffers and initialize
some phase index stuff. If this is a normal run the initial tracer
concentrations will be assigned from the TBLK or TVDPF keywords.
2. [Restart only:] The tracer concentration are read from the restart
file and the concentrations are applied with repeated calls to the
setTracerConcentration() method. This is currently done in the
eclwriter::beginRestart() method.
3. Internally the tracer model manages the concentrations in "batches" for
the oil, water and gas tracers respectively. The batches should be
initialized with the initial concentration, that must be performed
after the concentration values have been assigned. This is done in
method prepareTracerBatches() called from eclproblem::finishInit().
*/
void init(bool rst)
{
this->doInit(rst, simulator_.model().numGridDof(),
gasPhaseIdx, oilPhaseIdx, waterPhaseIdx);
}
void prepareTracerBatches()
{
for (std::size_t tracerIdx = 0; tracerIdx < this->tracerPhaseIdx_.size(); ++tracerIdx) {
if (this->tracerPhaseIdx_[tracerIdx] == FluidSystem::waterPhaseIdx) {
if (! FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)){
throw std::runtime_error("Water tracer specified for non-water fluid system:" + this->name(tracerIdx));
}
wat_.addTracer(tracerIdx, this->tracerConcentration_[tracerIdx]);
}
else if (this->tracerPhaseIdx_[tracerIdx] == FluidSystem::oilPhaseIdx) {
if (! FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)){
throw std::runtime_error("Oil tracer specified for non-oil fluid system:" + this->name(tracerIdx));
}
oil_.addTracer(tracerIdx, this->tracerConcentration_[tracerIdx]);
}
else if (this->tracerPhaseIdx_[tracerIdx] == FluidSystem::gasPhaseIdx) {
if (! FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)){
throw std::runtime_error("Gas tracer specified for non-gas fluid system:" + this->name(tracerIdx));
}
gas_.addTracer(tracerIdx, this->tracerConcentration_[tracerIdx]);
}
// resize free and solution volume storages
fVol1_[this->tracerPhaseIdx_[tracerIdx]].resize(this->freeTracerConcentration_[tracerIdx].size());
sVol1_[this->tracerPhaseIdx_[tracerIdx]].resize(this->solTracerConcentration_[tracerIdx].size());
dsVol_[this->tracerPhaseIdx_[tracerIdx]].resize(this->solTracerConcentration_[tracerIdx].size());
dfVol_[this->tracerPhaseIdx_[tracerIdx]].resize(this->solTracerConcentration_[tracerIdx].size());
}
// will be valid after we move out of tracerMatrix_
TracerMatrix* base = this->tracerMatrix_.get();
for (auto& tr : this->tbatch) {
if (tr.numTracer() != 0) {
if (this->tracerMatrix_)
tr.mat = std::move(this->tracerMatrix_);
else
tr.mat = std::make_unique<TracerMatrix>(*base);
}
}
}
void beginTimeStep()
{
if (this->numTracers() == 0)
return;
updateStorageCache();
}
/*!
* \brief Informs the tracer model that a time step has just been finished.
*/
void endTimeStep()
{
if (this->numTracers() == 0)
return;
advanceTracerFields();
}
/*!
* \brief This method writes the complete state of all tracer
* to the hard disk.
*/
template <class Restarter>
void serialize(Restarter&)
{ /* not implemented */ }
/*!
* \brief This method restores the complete state of the tracer
* from disk.
*
* It is the inverse of the serialize() method.
*/
template <class Restarter>
void deserialize(Restarter&)
{ /* not implemented */ }
template<class Serializer>
void serializeOp(Serializer& serializer)
{
serializer(static_cast<BaseType&>(*this));
serializer(tbatch);
}
protected:
// compute volume associated with free concentration
Scalar computeFreeVolume_(const int tracerPhaseIdx,
unsigned globalDofIdx,
unsigned timeIdx)
{
const auto& intQuants = simulator_.model().intensiveQuantities(globalDofIdx, timeIdx);
const auto& fs = intQuants.fluidState();
Scalar phaseVolume =
decay<Scalar>(fs.saturation(tracerPhaseIdx))
*decay<Scalar>(fs.invB(tracerPhaseIdx))
*decay<Scalar>(intQuants.porosity());
return max(phaseVolume, 1e-10);
}
// compute volume associated with solution concentration
Scalar computeSolutionVolume_(const int tracerPhaseIdx,
unsigned globalDofIdx,
unsigned timeIdx)
{
const auto& intQuants = simulator_.model().intensiveQuantities(globalDofIdx, timeIdx);
const auto& fs = intQuants.fluidState();
Scalar phaseVolume;
// vaporized oil
if (tracerPhaseIdx == FluidSystem::oilPhaseIdx && FluidSystem::enableVaporizedOil()) {
phaseVolume =
decay<Scalar>(fs.saturation(FluidSystem::gasPhaseIdx))
* decay<Scalar>(fs.invB(FluidSystem::gasPhaseIdx))
* decay<Scalar>(fs.Rv())
* decay<Scalar>(intQuants.porosity());
}
// dissolved gas
else if (tracerPhaseIdx == FluidSystem::gasPhaseIdx && FluidSystem::enableDissolvedGas()) {
phaseVolume =
decay<Scalar>(fs.saturation(FluidSystem::oilPhaseIdx))
* decay<Scalar>(fs.invB(FluidSystem::oilPhaseIdx))
* decay<Scalar>(fs.Rs())
* decay<Scalar>(intQuants.porosity());
}
else {
phaseVolume = 0.0;
}
return max(phaseVolume, 1e-10);
}
void computeFreeFlux_(TracerEvaluation & freeFlux,
bool & isUp,
const int tracerPhaseIdx,
const ElementContext& elemCtx,
unsigned scvfIdx,
unsigned timeIdx)
{
const auto& stencil = elemCtx.stencil(timeIdx);
const auto& scvf = stencil.interiorFace(scvfIdx);
const auto& extQuants = elemCtx.extensiveQuantities(scvfIdx, timeIdx);
unsigned inIdx = extQuants.interiorIndex();
unsigned upIdx = extQuants.upstreamIndex(tracerPhaseIdx);
const auto& intQuants = elemCtx.intensiveQuantities(upIdx, timeIdx);
const auto& fs = intQuants.fluidState();
Scalar v =
decay<Scalar>(extQuants.volumeFlux(tracerPhaseIdx))
* decay<Scalar>(fs.invB(tracerPhaseIdx));
Scalar A = scvf.area();
if (inIdx == upIdx) {
freeFlux = A*v*variable<TracerEvaluation>(1.0, 0);
isUp = true;
}
else {
freeFlux = A*v;
isUp = false;
}
}
void computeSolFlux_(TracerEvaluation & solFlux,
bool & isUp,
const int tracerPhaseIdx,
const ElementContext& elemCtx,
unsigned scvfIdx,
unsigned timeIdx)
{
const auto& stencil = elemCtx.stencil(timeIdx);
const auto& scvf = stencil.interiorFace(scvfIdx);
const auto& extQuants = elemCtx.extensiveQuantities(scvfIdx, timeIdx);
unsigned inIdx = extQuants.interiorIndex();
Scalar v;
unsigned upIdx;
// vaporized oil
if (tracerPhaseIdx == FluidSystem::oilPhaseIdx && FluidSystem::enableVaporizedOil()) {
upIdx = extQuants.upstreamIndex(FluidSystem::gasPhaseIdx);
const auto& intQuants = elemCtx.intensiveQuantities(upIdx, timeIdx);
const auto& fs = intQuants.fluidState();
v =
decay<Scalar>(fs.invB(FluidSystem::gasPhaseIdx))
* decay<Scalar>(extQuants.volumeFlux(FluidSystem::gasPhaseIdx))
* decay<Scalar>(fs.Rv());
}
// dissolved gas
else if (tracerPhaseIdx == FluidSystem::gasPhaseIdx && FluidSystem::enableDissolvedGas()) {
upIdx = extQuants.upstreamIndex(FluidSystem::oilPhaseIdx);
const auto& intQuants = elemCtx.intensiveQuantities(upIdx, timeIdx);
const auto& fs = intQuants.fluidState();
v =
decay<Scalar>(fs.invB(FluidSystem::oilPhaseIdx))
* decay<Scalar>(extQuants.volumeFlux(FluidSystem::oilPhaseIdx))
* decay<Scalar>(fs.Rs());
}
else {
upIdx = 0;
v = 0.0;
}
Scalar A = scvf.area();
if (inIdx == upIdx) {
solFlux = A*v*variable<TracerEvaluation>(1.0, 0);
isUp = true;
}
else {
solFlux = A*v;
isUp = false;
}
}
template<class TrRe>
void assembleTracerEquationVolume(TrRe& tr,
const ElementContext& elemCtx,
const Scalar scvVolume,
const Scalar dt,
unsigned I,
unsigned I1)
{
if (tr.numTracer() == 0)
return;
// Storage terms at previous time step (timeIdx = 1)
std::vector<Scalar> storageOfTimeIndex1(tr.numTracer());
std::vector<Scalar> fStorageOfTimeIndex1(tr.numTracer());
std::vector<Scalar> sStorageOfTimeIndex1(tr.numTracer());
if (elemCtx.enableStorageCache()) {
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
fStorageOfTimeIndex1[tIdx] = tr.storageOfTimeIndex1_[tIdx][I][0];
sStorageOfTimeIndex1[tIdx] = tr.storageOfTimeIndex1_[tIdx][I][1];
}
}
else {
Scalar fVolume1 = computeFreeVolume_(tr.phaseIdx_, I1, 1);
Scalar sVolume1 = computeSolutionVolume_(tr.phaseIdx_, I1, 1);
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
fStorageOfTimeIndex1[tIdx] = fVolume1 * tr.concentration_[tIdx][I1][0];
sStorageOfTimeIndex1[tIdx] = sVolume1 * tr.concentration_[tIdx][I1][1];
}
}
TracerEvaluation fVol = computeFreeVolume_(tr.phaseIdx_, I, 0) * variable<TracerEvaluation>(1.0, 0);
TracerEvaluation sVol = computeSolutionVolume_(tr.phaseIdx_, I, 0) * variable<TracerEvaluation>(1.0, 0);
dsVol_[tr.phaseIdx_][I] += sVol.value() * scvVolume - sVol1_[tr.phaseIdx_][I];
dfVol_[tr.phaseIdx_][I] += fVol.value() * scvVolume - fVol1_[tr.phaseIdx_][I];
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
// Free part
Scalar fStorageOfTimeIndex0 = fVol.value() * tr.concentration_[tIdx][I][0];
Scalar fLocalStorage = (fStorageOfTimeIndex0 - fStorageOfTimeIndex1[tIdx]) * scvVolume/dt;
tr.residual_[tIdx][I][0] += fLocalStorage; //residual + flux
// Solution part
Scalar sStorageOfTimeIndex0 = sVol.value() * tr.concentration_[tIdx][I][1];
Scalar sLocalStorage = (sStorageOfTimeIndex0 - sStorageOfTimeIndex1[tIdx]) * scvVolume/dt;
tr.residual_[tIdx][I][1] += sLocalStorage; //residual + flux
}
// Derivative matrix
(*tr.mat)[I][I][0][0] += fVol.derivative(0) * scvVolume/dt;
(*tr.mat)[I][I][1][1] += sVol.derivative(0) * scvVolume/dt;
}
template<class TrRe>
void assembleTracerEquationFlux(TrRe& tr,
const ElementContext& elemCtx,
unsigned scvfIdx,
unsigned I,
unsigned J,
const Scalar dt)
{
if (tr.numTracer() == 0)
return;
TracerEvaluation fFlux;
TracerEvaluation sFlux;
bool isUpF;
bool isUpS;
computeFreeFlux_(fFlux, isUpF, tr.phaseIdx_, elemCtx, scvfIdx, 0);
computeSolFlux_(sFlux, isUpS, tr.phaseIdx_, elemCtx, scvfIdx, 0);
dsVol_[tr.phaseIdx_][I] += sFlux.value() * dt;
dfVol_[tr.phaseIdx_][I] += fFlux.value() * dt;
int fGlobalUpIdx = isUpF ? I : J;
int sGlobalUpIdx = isUpS ? I : J;
for (int tIdx =0; tIdx < tr.numTracer(); ++tIdx) {
// Free and solution fluxes
tr.residual_[tIdx][I][0] += fFlux.value()*tr.concentration_[tIdx][fGlobalUpIdx][0]; //residual + flux
tr.residual_[tIdx][I][1] += sFlux.value()*tr.concentration_[tIdx][sGlobalUpIdx][1]; //residual + flux
}
// Derivative matrix
if (isUpF){
(*tr.mat)[J][I][0][0] = -fFlux.derivative(0);
(*tr.mat)[I][I][0][0] += fFlux.derivative(0);
}
if (isUpS) {
(*tr.mat)[J][I][1][1] = -sFlux.derivative(0);
(*tr.mat)[I][I][1][1] += sFlux.derivative(0);
}
}
template<class TrRe, class Well>
void assembleTracerEquationWell(TrRe& tr,
const Well& well)
{
if (tr.numTracer() == 0)
return;
const auto& eclWell = well.wellEcl();
// Init. well output to zero
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
this->wellTracerRate_[std::make_pair(eclWell.name(), this->name(tr.idx_[tIdx]))] = 0.0;
this->wellFreeTracerRate_[std::make_pair(eclWell.name(), this->wellfname(tr.idx_[tIdx]))] = 0.0;
this->wellSolTracerRate_[std::make_pair(eclWell.name(), this->wellsname(tr.idx_[tIdx]))] = 0.0;
if (eclWell.isMultiSegment()) {
for (std::size_t i = 0; i < eclWell.getConnections().size(); ++i) {
this->mSwTracerRate_[std::make_tuple(eclWell.name(),
this->name(tr.idx_[tIdx]),
eclWell.getConnections().get(i).segment())] = 0.0;
}
}
}
std::vector<Scalar> wtracer(tr.numTracer());
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
wtracer[tIdx] = this->currentConcentration_(eclWell, this->name(tr.idx_[tIdx]));
}
Scalar dt = simulator_.timeStepSize();
std::size_t well_index = simulator_.problem().wellModel().wellState().index(well.name()).value();
const auto& ws = simulator_.problem().wellModel().wellState().well(well_index);
for (std::size_t i = 0; i < ws.perf_data.size(); ++i) {
const auto I = ws.perf_data.cell_index[i];
Scalar rate = well.volumetricSurfaceRateForConnection(I, tr.phaseIdx_);
Scalar rate_s;
if (tr.phaseIdx_ == FluidSystem::oilPhaseIdx && FluidSystem::enableVaporizedOil()) {
rate_s = ws.perf_data.phase_mixing_rates[i][ws.vaporized_oil];
}
else if (tr.phaseIdx_ == FluidSystem::gasPhaseIdx && FluidSystem::enableDissolvedGas()) {
rate_s = ws.perf_data.phase_mixing_rates[i][ws.dissolved_gas];
}
else {
rate_s = 0.0;
}
Scalar rate_f = rate - rate_s;
if (rate_f > 0) {
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
// Injection of free tracer only
tr.residual_[tIdx][I][0] -= rate_f*wtracer[tIdx];
// Store _injector_ tracer rate for reporting (can be done here since WTRACER is constant)
this->wellTracerRate_.at(std::make_pair(eclWell.name(),this->name(tr.idx_[tIdx]))) += rate_f*wtracer[tIdx];
this->wellFreeTracerRate_.at(std::make_pair(eclWell.name(),this->wellfname(tr.idx_[tIdx]))) += rate_f*wtracer[tIdx];
if (eclWell.isMultiSegment()) {
this->mSwTracerRate_[std::make_tuple(eclWell.name(),
this->name(tr.idx_[tIdx]),
eclWell.getConnections().get(i).segment())] += rate_f*wtracer[tIdx];
}
}
dfVol_[tr.phaseIdx_][I] -= rate_f * dt;
}
else if (rate_f < 0) {
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
// Production of free tracer
tr.residual_[tIdx][I][0] -= rate_f * tr.concentration_[tIdx][I][0];
}
dfVol_[tr.phaseIdx_][I] -= rate_f * dt;
// Derivative matrix for free tracer producer
(*tr.mat)[I][I][0][0] -= rate_f * variable<TracerEvaluation>(1.0, 0).derivative(0);
}
if (rate_s < 0) {
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
// Production of solution tracer
tr.residual_[tIdx][I][1] -= rate_s * tr.concentration_[tIdx][I][1];
}
dsVol_[tr.phaseIdx_][I] -= rate_s * dt;
// Derivative matrix for solution tracer producer
(*tr.mat)[I][I][1][1] -= rate_s * variable<TracerEvaluation>(1.0, 0).derivative(0);
}
}
}
template<class TrRe>
void assembleTracerEquationSource(TrRe& tr,
const Scalar dt,
unsigned I)
{
if (tr.numTracer() == 0)
return;
// Skip if solution tracers do not exist
if (tr.phaseIdx_ == FluidSystem::waterPhaseIdx ||
(tr.phaseIdx_ == FluidSystem::gasPhaseIdx && !FluidSystem::enableDissolvedGas()) ||
(tr.phaseIdx_ == FluidSystem::oilPhaseIdx && !FluidSystem::enableVaporizedOil())) {
return;
}
const Scalar& dsVol = dsVol_[tr.phaseIdx_][I];
const Scalar& dfVol = dfVol_[tr.phaseIdx_][I];
// Source term determined by sign of dsVol: if dsVol > 0 then ms -> mf, else mf -> ms
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
if (dsVol >= 0) {
tr.residual_[tIdx][I][0] -= (dfVol / dt) * tr.concentration_[tIdx][I][0];
tr.residual_[tIdx][I][1] += (dfVol / dt) * tr.concentration_[tIdx][I][0];
}
else {
tr.residual_[tIdx][I][0] += (dsVol / dt) * tr.concentration_[tIdx][I][1];
tr.residual_[tIdx][I][1] -= (dsVol / dt) * tr.concentration_[tIdx][I][1];
}
}
// Derivative matrix
if (dsVol >= 0) {
(*tr.mat)[I][I][0][0] -= (dfVol / dt) * variable<TracerEvaluation>(1.0, 0).derivative(0);
(*tr.mat)[I][I][1][0] += (dfVol / dt) * variable<TracerEvaluation>(1.0, 0).derivative(0);
}
else {
(*tr.mat)[I][I][0][1] += (dsVol / dt) * variable<TracerEvaluation>(1.0, 0).derivative(0);
(*tr.mat)[I][I][1][1] -= (dsVol / dt) * variable<TracerEvaluation>(1.0, 0).derivative(0);
}
}
void assembleTracerEquations_()
{
// Note that we formulate the equations in terms of a concentration update
// (compared to previous time step) and not absolute concentration.
// This implies that current concentration (tr.concentration_[][]) contributes
// to the rhs both through storrage and flux terms.
// Compare also advanceTracerFields(...) below.
for (auto& tr : tbatch) {
if (tr.numTracer() != 0) {
(*tr.mat) = 0.0;
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
tr.residual_[tIdx] = 0.0;
}
}
}
// Well terms
const auto& wellPtrs = simulator_.problem().wellModel().localNonshutWells();
for (const auto& wellPtr : wellPtrs) {
for (auto& tr : tbatch) {
this->assembleTracerEquationWell(tr, *wellPtr);
}
}
ElementContext elemCtx(simulator_);
for (const auto& elem : elements(simulator_.gridView())) {
elemCtx.updateStencil(elem);
std::size_t I = elemCtx.globalSpaceIndex(/*dofIdx=*/ 0, /*timeIdx=*/0);
if (elem.partitionType() != Dune::InteriorEntity)
{
// Dirichlet boundary conditions needed for the parallel matrix
for (auto& tr : tbatch) {
if (tr.numTracer() != 0) {
(*tr.mat)[I][I][0][0] = 1.;
(*tr.mat)[I][I][1][1] = 1.;
}
}
continue;
}
elemCtx.updateAllIntensiveQuantities();
elemCtx.updateAllExtensiveQuantities();
Scalar extrusionFactor =
elemCtx.intensiveQuantities(/*dofIdx=*/ 0, /*timeIdx=*/0).extrusionFactor();
Valgrind::CheckDefined(extrusionFactor);
assert(isfinite(extrusionFactor));
assert(extrusionFactor > 0.0);
Scalar scvVolume =
elemCtx.stencil(/*timeIdx=*/0).subControlVolume(/*dofIdx=*/ 0).volume()
* extrusionFactor;
Scalar dt = elemCtx.simulator().timeStepSize();
std::size_t I1 = elemCtx.globalSpaceIndex(/*dofIdx=*/ 0, /*timeIdx=*/1);
for (auto& tr : tbatch) {
this->assembleTracerEquationVolume(tr, elemCtx, scvVolume, dt, I, I1);
}
std::size_t numInteriorFaces = elemCtx.numInteriorFaces(/*timIdx=*/0);
for (unsigned scvfIdx = 0; scvfIdx < numInteriorFaces; scvfIdx++) {
const auto& face = elemCtx.stencil(0).interiorFace(scvfIdx);
unsigned j = face.exteriorIndex();
unsigned J = elemCtx.globalSpaceIndex(/*dofIdx=*/ j, /*timIdx=*/0);
for (auto& tr : tbatch) {
this->assembleTracerEquationFlux(tr, elemCtx, scvfIdx, I, J, dt);
}
}
// Source terms (mass transfer between free and solution tracer)
for (auto& tr : tbatch) {
this->assembleTracerEquationSource(tr, dt, I);
}
}
// Communicate overlap using grid Communication
for (auto& tr : tbatch) {
if (tr.numTracer() == 0)
continue;
auto handle = VectorVectorDataHandle<GridView, std::vector<TracerVector>>(tr.residual_,
simulator_.gridView());
simulator_.gridView().communicate(handle, Dune::InteriorBorder_All_Interface,
Dune::ForwardCommunication);
}
}
void updateStorageCache()
{
for (auto& tr : tbatch) {
if (tr.numTracer() != 0) {
tr.concentrationInitial_ = tr.concentration_;
}
}
ElementContext elemCtx(simulator_);
for (const auto& elem : elements(simulator_.gridView())) {
elemCtx.updatePrimaryStencil(elem);
elemCtx.updatePrimaryIntensiveQuantities(/*timeIdx=*/0);
Scalar extrusionFactor = elemCtx.intensiveQuantities(/*dofIdx=*/ 0, /*timeIdx=*/0).extrusionFactor();
Scalar scvVolume = elemCtx.stencil(/*timeIdx=*/0).subControlVolume(/*dofIdx=*/ 0).volume() * extrusionFactor;
int globalDofIdx = elemCtx.globalSpaceIndex(0, /*timeIdx=*/0);
for (auto& tr : tbatch) {
if (tr.numTracer() == 0)
continue;
Scalar fVol1 = computeFreeVolume_(tr.phaseIdx_, globalDofIdx, 0);
Scalar sVol1 = computeSolutionVolume_(tr.phaseIdx_, globalDofIdx, 0);
fVol1_[tr.phaseIdx_][globalDofIdx] = fVol1 * scvVolume;
sVol1_[tr.phaseIdx_][globalDofIdx] = sVol1 * scvVolume;
dsVol_[tr.phaseIdx_][globalDofIdx] = 0.0;
dfVol_[tr.phaseIdx_][globalDofIdx] = 0.0;
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
tr.storageOfTimeIndex1_[tIdx][globalDofIdx][0] = fVol1 * tr.concentrationInitial_[tIdx][globalDofIdx][0];
tr.storageOfTimeIndex1_[tIdx][globalDofIdx][1] = sVol1 * tr.concentrationInitial_[tIdx][globalDofIdx][1];
}
}
}
}
void advanceTracerFields()
{
assembleTracerEquations_();
for (auto& tr : tbatch) {
if (tr.numTracer() == 0)
continue;
// Note that we solve for a concentration update (compared to previous time step)
// Confer also assembleTracerEquations_(...) above.
std::vector<TracerVector> dx(tr.concentration_);
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
dx[tIdx] = 0.0;
}
bool converged = this->linearSolveBatchwise_(*tr.mat, dx, tr.residual_);
if (!converged) {
OpmLog::warning("### Tracer model: Linear solver did not converge. ###");
}
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
for (std::size_t globalDofIdx = 0; globalDofIdx < tr.concentration_[tIdx].size(); ++globalDofIdx) {
// New concetration. Concentrations that are negative or where free/solution phase is not
// present are set to zero
const auto& intQuants = simulator_.model().intensiveQuantities(globalDofIdx, 0);
const auto& fs = intQuants.fluidState();
Scalar Sf = decay<Scalar>(fs.saturation(tr.phaseIdx_));
Scalar Ss = 0.0;
if (tr.phaseIdx_ == FluidSystem::gasPhaseIdx && FluidSystem::enableDissolvedGas())
Ss = decay<Scalar>(fs.saturation(FluidSystem::oilPhaseIdx));
else if (tr.phaseIdx_ == FluidSystem::oilPhaseIdx && FluidSystem::enableVaporizedOil())
Ss = decay<Scalar>(fs.saturation(FluidSystem::gasPhaseIdx));
const Scalar tol_gas_sat = 1e-6;
if ((tr.concentration_[tIdx][globalDofIdx][0] - dx[tIdx][globalDofIdx][0] < 0.0)
|| Sf < tol_gas_sat)
tr.concentration_[tIdx][globalDofIdx][0] = 0.0;
else
tr.concentration_[tIdx][globalDofIdx][0] -= dx[tIdx][globalDofIdx][0];
if (tr.concentration_[tIdx][globalDofIdx][1] - dx[tIdx][globalDofIdx][1] < 0.0
|| Ss < tol_gas_sat)
tr.concentration_[tIdx][globalDofIdx][1] = 0.0;
else
tr.concentration_[tIdx][globalDofIdx][1] -= dx[tIdx][globalDofIdx][1];
// Partition concentration into free and solution tracers for output
this->freeTracerConcentration_[tr.idx_[tIdx]][globalDofIdx] = tr.concentration_[tIdx][globalDofIdx][0];
this->solTracerConcentration_[tr.idx_[tIdx]][globalDofIdx] = tr.concentration_[tIdx][globalDofIdx][1];
}
}
// Store _producer_ tracer rate for reporting
const auto& wellPtrs = simulator_.problem().wellModel().localNonshutWells();
for (const auto& wellPtr : wellPtrs) {
const auto& eclWell = wellPtr->wellEcl();
// Injection rates already reported during assembly
if (!eclWell.isProducer())
continue;
Scalar rateWellPos = 0.0;
Scalar rateWellNeg = 0.0;
std::size_t well_index = simulator_.problem().wellModel().wellState().index(eclWell.name()).value();
const auto& ws = simulator_.problem().wellModel().wellState().well(well_index);
for (std::size_t i = 0; i < ws.perf_data.size(); ++i) {
const auto I = ws.perf_data.cell_index[i];
Scalar rate = wellPtr->volumetricSurfaceRateForConnection(I, tr.phaseIdx_);
Scalar rate_s;
if (tr.phaseIdx_ == FluidSystem::oilPhaseIdx && FluidSystem::enableVaporizedOil()) {
rate_s = ws.perf_data.phase_mixing_rates[i][ws.vaporized_oil];
}
else if (tr.phaseIdx_ == FluidSystem::gasPhaseIdx && FluidSystem::enableDissolvedGas()) {
rate_s = ws.perf_data.phase_mixing_rates[i][ws.dissolved_gas];
}
else {
rate_s = 0.0;
}
Scalar rate_f = rate - rate_s;
if (rate_f < 0) {
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
// Store _producer_ free tracer rate for reporting
this->wellTracerRate_.at(std::make_pair(eclWell.name(),this->name(tr.idx_[tIdx]))) +=
rate_f * tr.concentration_[tIdx][I][0];
this->wellFreeTracerRate_.at(std::make_pair(eclWell.name(),this->wellfname(tr.idx_[tIdx]))) +=
rate_f * tr.concentration_[tIdx][I][0];
if (eclWell.isMultiSegment()) {
this->mSwTracerRate_[std::make_tuple(eclWell.name(),
this->name(tr.idx_[tIdx]),
eclWell.getConnections().get(i).segment())] +=
rate_f * tr.concentration_[tIdx][I][0];
}
}
}
if (rate_s < 0) {
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
// Store _producer_ solution tracer rate for reporting
this->wellTracerRate_.at(std::make_pair(eclWell.name(),this->name(tr.idx_[tIdx]))) +=
rate_s * tr.concentration_[tIdx][I][1];
this->wellSolTracerRate_.at(std::make_pair(eclWell.name(),this->wellsname(tr.idx_[tIdx]))) +=
rate_s * tr.concentration_[tIdx][I][1];
if (eclWell.isMultiSegment()) {
this->mSwTracerRate_[std::make_tuple(eclWell.name(),
this->name(tr.idx_[tIdx]),
eclWell.getConnections().get(i).segment())] +=
rate_s * tr.concentration_[tIdx][I][1];
}
}
}
if (rate < 0) {
rateWellNeg += rate;
}
else {
rateWellPos += rate;
}
}
Scalar rateWellTotal = rateWellNeg + rateWellPos;
// TODO: Some inconsistencies here that perhaps should be clarified. The "offical" rate as reported below is
// occasionally significant different from the sum over connections (as calculated above). Only observed
// for small values, neglible for the rate itself, but matters when used to calculate tracer concentrations.
Scalar official_well_rate_total = simulator_.problem().wellModel().wellState().well(well_index).surface_rates[tr.phaseIdx_];
rateWellTotal = official_well_rate_total;
if (rateWellTotal > rateWellNeg) { // Cross flow
const Scalar bucketPrDay = 10.0/(1000.*3600.*24.); // ... keeps (some) trouble away
const Scalar factor = (rateWellTotal < -bucketPrDay) ? rateWellTotal/rateWellNeg : 0.0;
for (int tIdx = 0; tIdx < tr.numTracer(); ++tIdx) {
this->wellTracerRate_.at(std::make_pair(eclWell.name(),this->name(tr.idx_[tIdx]))) *= factor;
}
}
}
}
}
Simulator& simulator_;
// This struct collects tracers of the same type (i.e, transported in same phase).
// The idea being that, under the assumption of linearity, tracers of same type can
// be solved in concert, having a common system matrix but separate right-hand-sides.
// Since oil or gas tracers appears in dual compositions when VAPOIL respectively DISGAS
// is active, the template argument is intended to support future extension to these
// scenarios by supplying an extended vector type.
template <typename TV>
struct TracerBatch {
std::vector<int> idx_;
const int phaseIdx_;
std::vector<TV> concentrationInitial_;
std::vector<TV> concentration_;
std::vector<TV> storageOfTimeIndex1_;
std::vector<TV> residual_;
std::unique_ptr<TracerMatrix> mat;
bool operator==(const TracerBatch& rhs) const
{
return this->concentrationInitial_ == rhs.concentrationInitial_ &&
this->concentration_ == rhs.concentration_;
}
static TracerBatch serializationTestObject()
{
TracerBatch<TV> result(4);
result.idx_ = {1,2,3};
result.concentrationInitial_ = {5.0, 6.0};
result.concentration_ = {7.0, 8.0};
result.storageOfTimeIndex1_ = {9.0, 10.0, 11.0};
result.residual_ = {12.0, 13.0};
return result;
}
template<class Serializer>
void serializeOp(Serializer& serializer)
{
serializer(concentrationInitial_);
serializer(concentration_);
}
TracerBatch(int phaseIdx = 0) : phaseIdx_(phaseIdx) {}
int numTracer() const {return idx_.size(); }
void addTracer(const int idx, const TV & concentration)
{
int numGridDof = concentration.size();
idx_.emplace_back(idx);
concentrationInitial_.emplace_back(concentration);
concentration_.emplace_back(concentration);
residual_.emplace_back(numGridDof);
storageOfTimeIndex1_.emplace_back(numGridDof);
}
};
std::array<TracerBatch<TracerVector>,3> tbatch;
TracerBatch<TracerVector>& wat_;
TracerBatch<TracerVector>& oil_;
TracerBatch<TracerVector>& gas_;
std::array<std::vector<Scalar>, 3> fVol1_;
std::array<std::vector<Scalar>, 3> sVol1_;
std::array<std::vector<Scalar>, 3> dsVol_;
std::array<std::vector<Scalar>, 3> dfVol_;
};
} // namespace Opm
#endif // OPM_TRACER_MODEL_HPP
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