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3296 lines
139 KiB
C++
3296 lines
139 KiB
C++
/*
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Copyright 2017 SINTEF Digital, Mathematics and Cybernetics.
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Copyright 2017 Statoil ASA.
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Copyright 2016 - 2017 IRIS AS.
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This file is part of the Open Porous Media project (OPM).
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OPM is free software: you can redistribute it and/or modify
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it under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 3 of the License, or
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(at your option) any later version.
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OPM is distributed in the hope that it will be useful,
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but WITHOUT ANY WARRANTY; without even the implied warranty of
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MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the
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GNU General Public License for more details.
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You should have received a copy of the GNU General Public License
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along with OPM. If not, see <http://www.gnu.org/licenses/>.
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*/
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#include <opm/parser/eclipse/EclipseState/Schedule/Well/WellInjectionProperties.hpp>
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#include <opm/simulators/utils/DeferredLoggingErrorHelpers.hpp>
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namespace Opm
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{
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template<typename TypeTag>
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StandardWell<TypeTag>::
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StandardWell(const Well2& well, const int time_step, const Wells* wells,
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const ModelParameters& param,
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const RateConverterType& rate_converter,
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const int pvtRegionIdx,
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const int num_components)
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: Base(well, time_step, wells, param, rate_converter, pvtRegionIdx, num_components)
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, perf_densities_(number_of_perforations_)
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, perf_pressure_diffs_(number_of_perforations_)
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, F0_(numWellConservationEq)
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, ipr_a_(number_of_phases_)
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, ipr_b_(number_of_phases_)
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{
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assert(num_components_ == numWellConservationEq);
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duneB_.setBuildMode( OffDiagMatWell::row_wise );
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duneC_.setBuildMode( OffDiagMatWell::row_wise );
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invDuneD_.setBuildMode( DiagMatWell::row_wise );
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}
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template<typename TypeTag>
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void
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StandardWell<TypeTag>::
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init(const PhaseUsage* phase_usage_arg,
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const std::vector<double>& depth_arg,
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const double gravity_arg,
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const int num_cells)
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{
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Base::init(phase_usage_arg, depth_arg, gravity_arg, num_cells);
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perf_depth_.resize(number_of_perforations_, 0.);
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for (int perf = 0; perf < number_of_perforations_; ++perf) {
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const int cell_idx = well_cells_[perf];
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perf_depth_[perf] = depth_arg[cell_idx];
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}
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// counting/updating primary variable numbers
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if (this->has_polymermw && well_type_ == INJECTOR) {
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// adding a primary variable for water perforation rate per connection
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numWellEq_ += number_of_perforations_;
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// adding a primary variable for skin pressure per connection
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numWellEq_ += number_of_perforations_;
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}
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// with the updated numWellEq_, we can initialize the primary variables and matrices now
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primary_variables_.resize(numWellEq_, 0.0);
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primary_variables_evaluation_.resize(numWellEq_, EvalWell{numWellEq_ + numEq, 0.0});
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// setup sparsity pattern for the matrices
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//[A C^T [x = [ res
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// B D] x_well] res_well]
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// set the size of the matrices
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invDuneD_.setSize(1, 1, 1);
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duneB_.setSize(1, num_cells, number_of_perforations_);
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duneC_.setSize(1, num_cells, number_of_perforations_);
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for (auto row=invDuneD_.createbegin(), end = invDuneD_.createend(); row!=end; ++row) {
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// Add nonzeros for diagonal
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row.insert(row.index());
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}
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// the block size is run-time determined now
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invDuneD_[0][0].resize(numWellEq_, numWellEq_);
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for (auto row = duneB_.createbegin(), end = duneB_.createend(); row!=end; ++row) {
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for (int perf = 0 ; perf < number_of_perforations_; ++perf) {
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const int cell_idx = well_cells_[perf];
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row.insert(cell_idx);
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}
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}
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for (int perf = 0 ; perf < number_of_perforations_; ++perf) {
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const int cell_idx = well_cells_[perf];
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// the block size is run-time determined now
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duneB_[0][cell_idx].resize(numWellEq_, numEq);
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}
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// make the C^T matrix
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for (auto row = duneC_.createbegin(), end = duneC_.createend(); row!=end; ++row) {
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for (int perf = 0; perf < number_of_perforations_; ++perf) {
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const int cell_idx = well_cells_[perf];
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row.insert(cell_idx);
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}
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}
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for (int perf = 0; perf < number_of_perforations_; ++perf) {
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const int cell_idx = well_cells_[perf];
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duneC_[0][cell_idx].resize(numWellEq_, numEq);
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}
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resWell_.resize(1);
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// the block size of resWell_ is also run-time determined now
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resWell_[0].resize(numWellEq_);
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// resize temporary class variables
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Bx_.resize( duneB_.N() );
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for (unsigned i = 0; i < duneB_.N(); ++i) {
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Bx_[i].resize(numWellEq_);
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}
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invDrw_.resize( invDuneD_.N() );
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for (unsigned i = 0; i < invDuneD_.N(); ++i) {
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invDrw_[i].resize(numWellEq_);
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}
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}
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template<typename TypeTag>
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void StandardWell<TypeTag>::
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initPrimaryVariablesEvaluation() const
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{
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for (int eqIdx = 0; eqIdx < numWellEq_; ++eqIdx) {
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primary_variables_evaluation_[eqIdx] =
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EvalWell::createVariable(numWellEq_ + numEq, primary_variables_[eqIdx], numEq + eqIdx);
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}
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}
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template<typename TypeTag>
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const typename StandardWell<TypeTag>::EvalWell&
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StandardWell<TypeTag>::
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getBhp() const
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{
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return primary_variables_evaluation_[Bhp];
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}
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template<typename TypeTag>
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const typename StandardWell<TypeTag>::EvalWell&
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StandardWell<TypeTag>::
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getWQTotal() const
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{
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return primary_variables_evaluation_[WQTotal];
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}
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template<typename TypeTag>
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typename StandardWell<TypeTag>::EvalWell
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StandardWell<TypeTag>::
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getQs(const int comp_idx) const
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{
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// Note: currently, the WQTotal definition is still depends on Injector/Producer.
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assert(comp_idx < num_components_);
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if (well_type_ == INJECTOR) { // only single phase injection
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// TODO: using comp_frac here is dangerous, it should be changed later
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// Most likely, it should be changed to use distr, or at least, we need to update comp_frac_ based on distr
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// while solvent might complicate the situation
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const auto pu = phaseUsage();
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const int legacyCompIdx = ebosCompIdxToFlowCompIdx(comp_idx);
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double comp_frac = 0.0;
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if (has_solvent && comp_idx == contiSolventEqIdx) { // solvent
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comp_frac = comp_frac_[pu.phase_pos[ Gas ]] * wsolvent();
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} else if (legacyCompIdx == pu.phase_pos[ Gas ]) {
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comp_frac = comp_frac_[legacyCompIdx];
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if (has_solvent) {
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comp_frac *= (1.0 - wsolvent());
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}
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} else {
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comp_frac = comp_frac_[legacyCompIdx];
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}
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return comp_frac * primary_variables_evaluation_[WQTotal];
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} else { // producers
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return primary_variables_evaluation_[WQTotal] * wellVolumeFractionScaled(comp_idx);
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}
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}
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template<typename TypeTag>
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typename StandardWell<TypeTag>::EvalWell
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StandardWell<TypeTag>::
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wellVolumeFractionScaled(const int compIdx) const
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{
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const int legacyCompIdx = ebosCompIdxToFlowCompIdx(compIdx);
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const double scal = scalingFactor(legacyCompIdx);
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if (scal > 0)
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return wellVolumeFraction(compIdx) / scal;
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// the scaling factor may be zero for RESV controlled wells.
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return wellVolumeFraction(compIdx);
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}
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template<typename TypeTag>
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typename StandardWell<TypeTag>::EvalWell
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StandardWell<TypeTag>::
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wellVolumeFraction(const unsigned compIdx) const
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{
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if (FluidSystem::numActivePhases() == 1) {
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return EvalWell(numWellEq_ + numEq, 1.0);
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}
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if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx) && compIdx == Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx)) {
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return primary_variables_evaluation_[WFrac];
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}
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if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx) && compIdx == Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx)) {
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return primary_variables_evaluation_[GFrac];
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}
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if (has_solvent && compIdx == (unsigned)contiSolventEqIdx) {
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return primary_variables_evaluation_[SFrac];
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}
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// Oil fraction
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EvalWell well_fraction(numWellEq_ + numEq, 1.0);
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if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
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well_fraction -= primary_variables_evaluation_[WFrac];
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}
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if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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well_fraction -= primary_variables_evaluation_[GFrac];
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}
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if (has_solvent) {
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well_fraction -= primary_variables_evaluation_[SFrac];
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}
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return well_fraction;
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}
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template<typename TypeTag>
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typename StandardWell<TypeTag>::EvalWell
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StandardWell<TypeTag>::
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wellSurfaceVolumeFraction(const int compIdx) const
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{
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EvalWell sum_volume_fraction_scaled(numWellEq_ + numEq, 0.);
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for (int idx = 0; idx < num_components_; ++idx) {
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sum_volume_fraction_scaled += wellVolumeFractionScaled(idx);
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}
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assert(sum_volume_fraction_scaled.value() != 0.);
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return wellVolumeFractionScaled(compIdx) / sum_volume_fraction_scaled;
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}
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template<typename TypeTag>
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typename StandardWell<TypeTag>::EvalWell
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StandardWell<TypeTag>::
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extendEval(const Eval& in) const
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{
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EvalWell out(numWellEq_ + numEq, in.value());
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for(int eqIdx = 0; eqIdx < numEq;++eqIdx) {
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out.setDerivative(eqIdx, in.derivative(eqIdx));
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}
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return out;
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}
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template<typename TypeTag>
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typename StandardWell<TypeTag>::Eval
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StandardWell<TypeTag>::getPerfCellPressure(const typename StandardWell<TypeTag>::FluidState& fs) const
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{
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Eval pressure;
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if (Indices::oilEnabled) {
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pressure = fs.pressure(FluidSystem::oilPhaseIdx);
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} else {
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if (Indices::waterEnabled) {
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pressure = fs.pressure(FluidSystem::waterPhaseIdx);
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} else {
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pressure = fs.pressure(FluidSystem::gasPhaseIdx);
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}
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}
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return pressure;
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}
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template<typename TypeTag>
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void
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StandardWell<TypeTag>::
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computePerfRate(const IntensiveQuantities& intQuants,
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const std::vector<EvalWell>& mob,
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const EvalWell& bhp,
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const double Tw,
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const int perf,
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const bool allow_cf,
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std::vector<EvalWell>& cq_s,
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double& perf_dis_gas_rate,
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double& perf_vap_oil_rate,
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Opm::DeferredLogger& deferred_logger) const
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{
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const auto& fs = intQuants.fluidState();
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const EvalWell pressure = extendEval(getPerfCellPressure(fs));
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const EvalWell rs = extendEval(fs.Rs());
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const EvalWell rv = extendEval(fs.Rv());
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std::vector<EvalWell> b_perfcells_dense(num_components_, EvalWell{numWellEq_ + numEq, 0.0});
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for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++phaseIdx) {
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if (!FluidSystem::phaseIsActive(phaseIdx)) {
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continue;
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}
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const unsigned compIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::solventComponentIndex(phaseIdx));
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b_perfcells_dense[compIdx] = extendEval(fs.invB(phaseIdx));
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}
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if (has_solvent) {
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b_perfcells_dense[contiSolventEqIdx] = extendEval(intQuants.solventInverseFormationVolumeFactor());
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}
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// Pressure drawdown (also used to determine direction of flow)
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const EvalWell well_pressure = bhp + perf_pressure_diffs_[perf];
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EvalWell drawdown = pressure - well_pressure;
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if (this->has_polymermw && well_type_ == INJECTOR) {
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const int pskin_index = Bhp + 1 + number_of_perforations_ + perf;
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const EvalWell& skin_pressure = primary_variables_evaluation_[pskin_index];
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drawdown += skin_pressure;
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}
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// producing perforations
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if ( drawdown.value() > 0 ) {
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//Do nothing if crossflow is not allowed
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if (!allow_cf && well_type_ == INJECTOR) {
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return;
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}
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// compute component volumetric rates at standard conditions
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for (int componentIdx = 0; componentIdx < num_components_; ++componentIdx) {
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const EvalWell cq_p = - Tw * (mob[componentIdx] * drawdown);
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cq_s[componentIdx] = b_perfcells_dense[componentIdx] * cq_p;
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}
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if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) && FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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const unsigned oilCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
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const unsigned gasCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
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const EvalWell cq_sOil = cq_s[oilCompIdx];
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const EvalWell cq_sGas = cq_s[gasCompIdx];
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const EvalWell dis_gas = rs * cq_sOil;
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const EvalWell vap_oil = rv * cq_sGas;
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cq_s[gasCompIdx] += dis_gas;
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cq_s[oilCompIdx] += vap_oil;
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// recording the perforation solution gas rate and solution oil rates
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if (well_type_ == PRODUCER) {
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perf_dis_gas_rate = dis_gas.value();
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perf_vap_oil_rate = vap_oil.value();
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}
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}
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} else {
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//Do nothing if crossflow is not allowed
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if (!allow_cf && well_type_ == PRODUCER) {
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return;
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}
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// Using total mobilities
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EvalWell total_mob_dense = mob[0];
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for (int componentIdx = 1; componentIdx < num_components_; ++componentIdx) {
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total_mob_dense += mob[componentIdx];
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}
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// injection perforations total volume rates
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const EvalWell cqt_i = - Tw * (total_mob_dense * drawdown);
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// surface volume fraction of fluids within wellbore
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std::vector<EvalWell> cmix_s(num_components_, EvalWell{numWellEq_ + numEq});
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for (int componentIdx = 0; componentIdx < num_components_; ++componentIdx) {
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cmix_s[componentIdx] = wellSurfaceVolumeFraction(componentIdx);
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}
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// compute volume ratio between connection at standard conditions
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EvalWell volumeRatio(numWellEq_ + numEq, 0.);
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if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
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const unsigned waterCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx);
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volumeRatio += cmix_s[waterCompIdx] / b_perfcells_dense[waterCompIdx];
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}
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if (has_solvent) {
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volumeRatio += cmix_s[contiSolventEqIdx] / b_perfcells_dense[contiSolventEqIdx];
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}
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if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) && FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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const unsigned oilCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
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const unsigned gasCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
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// Incorporate RS/RV factors if both oil and gas active
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const EvalWell d = EvalWell(numWellEq_ + numEq, 1.0) - rv * rs;
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if (d.value() == 0.0) {
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OPM_DEFLOG_THROW(Opm::NumericalIssue, "Zero d value obtained for well " << name() << " during flux calcuation"
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<< " with rs " << rs << " and rv " << rv, deferred_logger);
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}
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const EvalWell tmp_oil = (cmix_s[oilCompIdx] - rv * cmix_s[gasCompIdx]) / d;
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//std::cout << "tmp_oil " <<tmp_oil << std::endl;
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volumeRatio += tmp_oil / b_perfcells_dense[oilCompIdx];
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const EvalWell tmp_gas = (cmix_s[gasCompIdx] - rs * cmix_s[oilCompIdx]) / d;
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//std::cout << "tmp_gas " <<tmp_gas << std::endl;
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volumeRatio += tmp_gas / b_perfcells_dense[gasCompIdx];
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}
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else {
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if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
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const unsigned oilCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
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volumeRatio += cmix_s[oilCompIdx] / b_perfcells_dense[oilCompIdx];
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}
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if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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const unsigned gasCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
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volumeRatio += cmix_s[gasCompIdx] / b_perfcells_dense[gasCompIdx];
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}
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}
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// injecting connections total volumerates at standard conditions
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EvalWell cqt_is = cqt_i/volumeRatio;
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//std::cout << "volrat " << volumeRatio << " " << volrat_perf_[perf] << std::endl;
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for (int componentIdx = 0; componentIdx < num_components_; ++componentIdx) {
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cq_s[componentIdx] = cmix_s[componentIdx] * cqt_is; // * b_perfcells_dense[phase];
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}
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// calculating the perforation solution gas rate and solution oil rates
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if (well_type_ == PRODUCER) {
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if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) && FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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const unsigned oilCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
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const unsigned gasCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
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// TODO: the formulations here remain to be tested with cases with strong crossflow through production wells
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// s means standard condition, r means reservoir condition
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// q_os = q_or * b_o + rv * q_gr * b_g
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// q_gs = q_gr * g_g + rs * q_or * b_o
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// d = 1.0 - rs * rv
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// q_or = 1 / (b_o * d) * (q_os - rv * q_gs)
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// q_gr = 1 / (b_g * d) * (q_gs - rs * q_os)
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const double d = 1.0 - rv.value() * rs.value();
|
|
// vaporized oil into gas
|
|
// rv * q_gr * b_g = rv * (q_gs - rs * q_os) / d
|
|
perf_vap_oil_rate = rv.value() * (cq_s[gasCompIdx].value() - rs.value() * cq_s[oilCompIdx].value()) / d;
|
|
// dissolved of gas in oil
|
|
// rs * q_or * b_o = rs * (q_os - rv * q_gs) / d
|
|
perf_dis_gas_rate = rs.value() * (cq_s[oilCompIdx].value() - rv.value() * cq_s[gasCompIdx].value()) / d;
|
|
}
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
assembleWellEq(const Simulator& ebosSimulator,
|
|
const std::vector<Scalar>& /* B_avg */,
|
|
const double dt,
|
|
WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
// TODO: only_wells should be put back to save some computation
|
|
// for example, the matrices B C does not need to update if only_wells
|
|
|
|
checkWellOperability(ebosSimulator, well_state, deferred_logger);
|
|
|
|
if (!this->isOperable()) return;
|
|
|
|
// clear all entries
|
|
duneB_ = 0.0;
|
|
duneC_ = 0.0;
|
|
invDuneD_ = 0.0;
|
|
resWell_ = 0.0;
|
|
|
|
// TODO: it probably can be static member for StandardWell
|
|
const double volume = 0.002831684659200; // 0.1 cu ft;
|
|
|
|
const bool allow_cf = getAllowCrossFlow() || openCrossFlowAvoidSingularity(ebosSimulator);
|
|
|
|
const EvalWell& bhp = getBhp();
|
|
|
|
// the solution gas rate and solution oil rate needs to be reset to be zero for well_state.
|
|
well_state.wellVaporizedOilRates()[index_of_well_] = 0.;
|
|
well_state.wellDissolvedGasRates()[index_of_well_] = 0.;
|
|
|
|
const int np = number_of_phases_;
|
|
for (int p = 0; p < np; ++p) {
|
|
well_state.productivityIndex()[np*index_of_well_ + p] = 0.;
|
|
}
|
|
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
|
|
const int cell_idx = well_cells_[perf];
|
|
const auto& intQuants = *(ebosSimulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/ 0));
|
|
std::vector<EvalWell> mob(num_components_, {numWellEq_ + numEq, 0.});
|
|
getMobility(ebosSimulator, perf, mob, deferred_logger);
|
|
|
|
std::vector<EvalWell> cq_s(num_components_, {numWellEq_ + numEq, 0.});
|
|
double perf_dis_gas_rate = 0.;
|
|
double perf_vap_oil_rate = 0.;
|
|
double trans_mult = ebosSimulator.problem().template rockCompTransMultiplier<double>(intQuants, cell_idx);
|
|
const double Tw = well_index_[perf] * trans_mult;
|
|
computePerfRate(intQuants, mob, bhp, Tw, perf, allow_cf,
|
|
cq_s, perf_dis_gas_rate, perf_vap_oil_rate, deferred_logger);
|
|
|
|
// better way to do here is that use the cq_s and then replace the cq_s_water here?
|
|
if (has_polymer && this->has_polymermw && well_type_ == INJECTOR) {
|
|
handleInjectivityRateAndEquations(intQuants, well_state, perf, cq_s, deferred_logger);
|
|
}
|
|
|
|
// updating the solution gas rate and solution oil rate
|
|
if (well_type_ == PRODUCER) {
|
|
well_state.wellDissolvedGasRates()[index_of_well_] += perf_dis_gas_rate;
|
|
well_state.wellVaporizedOilRates()[index_of_well_] += perf_vap_oil_rate;
|
|
}
|
|
|
|
if (has_energy) {
|
|
connectionRates_[perf][contiEnergyEqIdx] = 0.0;
|
|
}
|
|
|
|
for (int componentIdx = 0; componentIdx < num_components_; ++componentIdx) {
|
|
// the cq_s entering mass balance equations need to consider the efficiency factors.
|
|
const EvalWell cq_s_effective = cq_s[componentIdx] * well_efficiency_factor_;
|
|
|
|
connectionRates_[perf][componentIdx] = Base::restrictEval(cq_s_effective);
|
|
|
|
// subtract sum of phase fluxes in the well equations.
|
|
resWell_[0][componentIdx] += cq_s_effective.value();
|
|
|
|
// assemble the jacobians
|
|
for (int pvIdx = 0; pvIdx < numWellEq_; ++pvIdx) {
|
|
// also need to consider the efficiency factor when manipulating the jacobians.
|
|
duneC_[0][cell_idx][pvIdx][componentIdx] -= cq_s_effective.derivative(pvIdx+numEq); // intput in transformed matrix
|
|
invDuneD_[0][0][componentIdx][pvIdx] += cq_s_effective.derivative(pvIdx+numEq);
|
|
}
|
|
|
|
for (int pvIdx = 0; pvIdx < numEq; ++pvIdx) {
|
|
duneB_[0][cell_idx][componentIdx][pvIdx] += cq_s_effective.derivative(pvIdx);
|
|
}
|
|
|
|
// Store the perforation phase flux for later usage.
|
|
if (has_solvent && componentIdx == contiSolventEqIdx) {
|
|
well_state.perfRateSolvent()[first_perf_ + perf] = cq_s[componentIdx].value();
|
|
} else {
|
|
well_state.perfPhaseRates()[(first_perf_ + perf) * np + ebosCompIdxToFlowCompIdx(componentIdx)] = cq_s[componentIdx].value();
|
|
}
|
|
}
|
|
if (has_energy) {
|
|
|
|
auto fs = intQuants.fluidState();
|
|
for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++phaseIdx) {
|
|
if (!FluidSystem::phaseIsActive(phaseIdx)) {
|
|
continue;
|
|
}
|
|
|
|
const unsigned activeCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::solventComponentIndex(phaseIdx));
|
|
// convert to reservoar conditions
|
|
EvalWell cq_r_thermal(numWellEq_ + numEq, 0.);
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) && FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
|
|
if(FluidSystem::waterPhaseIdx == phaseIdx)
|
|
cq_r_thermal = cq_s[activeCompIdx] / extendEval(fs.invB(phaseIdx));
|
|
|
|
// remove dissolved gas and vapporized oil
|
|
const unsigned oilCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
|
|
const unsigned gasCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
|
|
// q_os = q_or * b_o + rv * q_gr * b_g
|
|
// q_gs = q_gr * g_g + rs * q_or * b_o
|
|
// d = 1.0 - rs * rv
|
|
const EvalWell d = extendEval(1.0 - fs.Rv() * fs.Rs());
|
|
// q_gr = 1 / (b_g * d) * (q_gs - rs * q_os)
|
|
if(FluidSystem::gasPhaseIdx == phaseIdx)
|
|
cq_r_thermal = (cq_s[gasCompIdx] - extendEval(fs.Rs()) * cq_s[oilCompIdx]) / (d * extendEval(fs.invB(phaseIdx)) );
|
|
// q_or = 1 / (b_o * d) * (q_os - rv * q_gs)
|
|
if(FluidSystem::oilPhaseIdx == phaseIdx)
|
|
cq_r_thermal = (cq_s[oilCompIdx] - extendEval(fs.Rv()) * cq_s[gasCompIdx]) / (d * extendEval(fs.invB(phaseIdx)) );
|
|
|
|
} else {
|
|
cq_r_thermal = cq_s[activeCompIdx] / extendEval(fs.invB(phaseIdx));
|
|
}
|
|
|
|
// change temperature for injecting fluids
|
|
if (well_type_ == INJECTOR && cq_s[activeCompIdx] > 0.0){
|
|
// only handles single phase injection now
|
|
assert(this->well_ecl_.injectorType() != Well2::InjectorType::MULTI);
|
|
fs.setTemperature(this->well_ecl_.temperature());
|
|
typedef typename std::decay<decltype(fs)>::type::Scalar FsScalar;
|
|
typename FluidSystem::template ParameterCache<FsScalar> paramCache;
|
|
const unsigned pvtRegionIdx = intQuants.pvtRegionIndex();
|
|
paramCache.setRegionIndex(pvtRegionIdx);
|
|
paramCache.setMaxOilSat(ebosSimulator.problem().maxOilSaturation(cell_idx));
|
|
paramCache.updatePhase(fs, phaseIdx);
|
|
|
|
const auto& rho = FluidSystem::density(fs, paramCache, phaseIdx);
|
|
fs.setDensity(phaseIdx, rho);
|
|
const auto& h = FluidSystem::enthalpy(fs, paramCache, phaseIdx);
|
|
fs.setEnthalpy(phaseIdx, h);
|
|
}
|
|
// compute the thermal flux
|
|
cq_r_thermal *= extendEval(fs.enthalpy(phaseIdx)) * extendEval(fs.density(phaseIdx));
|
|
connectionRates_[perf][contiEnergyEqIdx] += Base::restrictEval(cq_r_thermal);
|
|
}
|
|
}
|
|
|
|
if (has_polymer) {
|
|
// TODO: the application of well efficiency factor has not been tested with an example yet
|
|
const unsigned waterCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx);
|
|
EvalWell cq_s_poly = cq_s[waterCompIdx] * well_efficiency_factor_;
|
|
if (well_type_ == INJECTOR) {
|
|
cq_s_poly *= wpolymer();
|
|
} else {
|
|
cq_s_poly *= extendEval(intQuants.polymerConcentration() * intQuants.polymerViscosityCorrection());
|
|
}
|
|
connectionRates_[perf][contiPolymerEqIdx] = Base::restrictEval(cq_s_poly);
|
|
|
|
if (this->has_polymermw) {
|
|
updateConnectionRatePolyMW(cq_s_poly, intQuants, well_state, perf, deferred_logger);
|
|
}
|
|
}
|
|
|
|
if (has_foam) {
|
|
// TODO: the application of well efficiency factor has not been tested with an example yet
|
|
const unsigned gasCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
|
|
EvalWell cq_s_foam = cq_s[gasCompIdx] * well_efficiency_factor_;
|
|
if (well_type_ == INJECTOR) {
|
|
cq_s_foam *= wfoam();
|
|
} else {
|
|
cq_s_foam *= extendEval(intQuants.foamConcentration());
|
|
}
|
|
connectionRates_[perf][contiFoamEqIdx] = Base::restrictEval(cq_s_foam);
|
|
}
|
|
|
|
// Store the perforation pressure for later usage.
|
|
well_state.perfPress()[first_perf_ + perf] = well_state.bhp()[index_of_well_] + perf_pressure_diffs_[perf];
|
|
|
|
// Compute Productivity index if asked for
|
|
const auto& pu = phaseUsage();
|
|
const Opm::SummaryConfig& summaryConfig = ebosSimulator.vanguard().summaryConfig();
|
|
const Opm::Schedule& schedule = ebosSimulator.vanguard().schedule();
|
|
for (int p = 0; p < np; ++p) {
|
|
if ( (pu.phase_pos[Water] == p && (summaryConfig.hasSummaryKey("WPIW:" + name()) || summaryConfig.hasSummaryKey("WPIL:" + name())))
|
|
|| (pu.phase_pos[Oil] == p && (summaryConfig.hasSummaryKey("WPIO:" + name()) || summaryConfig.hasSummaryKey("WPIL:" + name())))
|
|
|| (pu.phase_pos[Gas] == p && summaryConfig.hasSummaryKey("WPIG:" + name()))) {
|
|
|
|
const unsigned int compIdx = flowPhaseToEbosCompIdx(p);
|
|
const auto& fs = intQuants.fluidState();
|
|
Eval perf_pressure = getPerfCellPressure(fs);
|
|
const double drawdown = well_state.perfPress()[first_perf_ + perf] - perf_pressure.value();
|
|
const bool new_well = schedule.hasWellEvent(name(), ScheduleEvents::NEW_WELL, current_step_);
|
|
double productivity_index = cq_s[compIdx].value() / drawdown;
|
|
scaleProductivityIndex(perf, productivity_index, new_well, deferred_logger);
|
|
well_state.productivityIndex()[np*index_of_well_ + p] += productivity_index;
|
|
}
|
|
}
|
|
|
|
}
|
|
|
|
// add vol * dF/dt + Q to the well equations;
|
|
for (int componentIdx = 0; componentIdx < numWellConservationEq; ++componentIdx) {
|
|
// TODO: following the development in MSW, we need to convert the volume of the wellbore to be surface volume
|
|
// since all the rates are under surface condition
|
|
EvalWell resWell_loc(numWellEq_ + numEq, 0.0);
|
|
if (FluidSystem::numActivePhases() > 1) {
|
|
assert(dt > 0);
|
|
resWell_loc += (wellSurfaceVolumeFraction(componentIdx) - F0_[componentIdx]) * volume / dt;
|
|
}
|
|
resWell_loc -= getQs(componentIdx) * well_efficiency_factor_;
|
|
for (int pvIdx = 0; pvIdx < numWellEq_; ++pvIdx) {
|
|
invDuneD_[0][0][componentIdx][pvIdx] += resWell_loc.derivative(pvIdx+numEq);
|
|
}
|
|
resWell_[0][componentIdx] += resWell_loc.value();
|
|
}
|
|
|
|
assembleControlEq(deferred_logger);
|
|
|
|
// do the local inversion of D.
|
|
try {
|
|
Dune::ISTLUtility::invertMatrix(invDuneD_[0][0]);
|
|
} catch( ... ) {
|
|
OPM_DEFLOG_THROW(Opm::NumericalIssue,"Error when inverting local well equations for well " + name(), deferred_logger);
|
|
}
|
|
|
|
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
assembleControlEq(Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
EvalWell control_eq(numWellEq_ + numEq, 0.);
|
|
switch (well_controls_get_current_type(well_controls_)) {
|
|
case THP:
|
|
{
|
|
std::vector<EvalWell> rates(3, {numWellEq_ + numEq, 0.});
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
rates[ Water ] = getQs(flowPhaseToEbosCompIdx(Water));
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
rates[ Oil ] = getQs(flowPhaseToEbosCompIdx(Oil));
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
rates[ Gas ] = getQs(flowPhaseToEbosCompIdx(Gas));
|
|
}
|
|
const int current = well_controls_get_current(well_controls_);
|
|
control_eq = getBhp() - calculateBhpFromThp(rates, current, deferred_logger);
|
|
break;
|
|
}
|
|
case BHP:
|
|
{
|
|
const double target_bhp = well_controls_get_current_target(well_controls_);
|
|
control_eq = getBhp() - target_bhp;
|
|
break;
|
|
}
|
|
case SURFACE_RATE:
|
|
{
|
|
const double target_rate = well_controls_get_current_target(well_controls_); // surface rate target
|
|
if (well_type_ == INJECTOR) {
|
|
control_eq = getWQTotal() - target_rate;
|
|
} else if (well_type_ == PRODUCER) {
|
|
if (target_rate != 0.) {
|
|
EvalWell rate_for_control(numWellEq_ + numEq, 0.);
|
|
const EvalWell& g_total = getWQTotal();
|
|
// a variable to check if we are producing any targeting fluids
|
|
double sum_fraction = 0.;
|
|
const double* distr = well_controls_get_current_distr(well_controls_);
|
|
for (int phase = 0; phase < number_of_phases_; ++phase) {
|
|
if (distr[phase] > 0.) {
|
|
const EvalWell fraction_scaled = wellVolumeFractionScaled(flowPhaseToEbosCompIdx(phase));
|
|
rate_for_control += g_total * fraction_scaled;
|
|
sum_fraction += fraction_scaled.value();
|
|
}
|
|
}
|
|
if (sum_fraction > 0.) {
|
|
control_eq = rate_for_control - target_rate;
|
|
} else {
|
|
// we are not producing any fluids that specfied for a non-zero target
|
|
// which makes it a mission impossible, we will set all the rates to be zero for this case
|
|
const std::string msg = " Setting all rates to be zero for well " + name()
|
|
+ " due to un-solvable situation. There is non-zero target for the phase "
|
|
+ " that does not exist in the wellbore for the situation";
|
|
deferred_logger.warning("NON_SOLVABLE_WELL_SOLUTION", msg);
|
|
|
|
control_eq = getWQTotal() - target_rate;
|
|
}
|
|
} else {
|
|
// there is some special treatment for the zero rate control well
|
|
// 1. if the well can produce the specified phase, it means the well should not produce any fluid, this
|
|
// is a fine situation.
|
|
// 2. if the well can not produce the specified phase, it cause a under-determined problem, we
|
|
// basically assume the well not producing any fluid as a solution
|
|
// With both the situation, we can use the following well equation
|
|
control_eq = getWQTotal() - target_rate;
|
|
}
|
|
}
|
|
break;
|
|
}
|
|
case RESERVOIR_RATE:
|
|
{
|
|
const double target_rate = well_controls_get_current_target(well_controls_); // reservoir rate target
|
|
if (well_type_ == INJECTOR) {
|
|
const double* distr = well_controls_get_current_distr(well_controls_);
|
|
for (int phase = 0; phase < number_of_phases_; ++phase) {
|
|
if (distr[phase] > 0.0) {
|
|
control_eq = getWQTotal() * scalingFactor(phase) - target_rate;
|
|
break;
|
|
}
|
|
}
|
|
} else {
|
|
const EvalWell& g_total = getWQTotal();
|
|
EvalWell rate_for_control(numWellEq_ + numEq, 0.); // reservoir rate
|
|
for (int phase = 0; phase < number_of_phases_; ++phase) {
|
|
rate_for_control += g_total * wellVolumeFraction( flowPhaseToEbosCompIdx(phase) );
|
|
}
|
|
control_eq = rate_for_control - target_rate;
|
|
}
|
|
break;
|
|
}
|
|
default:
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Unknown well control control types for well " << name(), deferred_logger);
|
|
}
|
|
|
|
// using control_eq to update the matrix and residuals
|
|
// TODO: we should use a different index system for the well equations
|
|
resWell_[0][Bhp] = control_eq.value();
|
|
for (int pv_idx = 0; pv_idx < numWellEq_; ++pv_idx) {
|
|
invDuneD_[0][0][Bhp][pv_idx] = control_eq.derivative(pv_idx + numEq);
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
getMobility(const Simulator& ebosSimulator,
|
|
const int perf,
|
|
std::vector<EvalWell>& mob,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
const int cell_idx = well_cells_[perf];
|
|
assert (int(mob.size()) == num_components_);
|
|
const auto& intQuants = *(ebosSimulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/0));
|
|
const auto& materialLawManager = ebosSimulator.problem().materialLawManager();
|
|
|
|
// either use mobility of the perforation cell or calcualte its own
|
|
// based on passing the saturation table index
|
|
const int satid = saturation_table_number_[perf] - 1;
|
|
const int satid_elem = materialLawManager->satnumRegionIdx(cell_idx);
|
|
if( satid == satid_elem ) { // the same saturation number is used. i.e. just use the mobilty from the cell
|
|
|
|
for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++phaseIdx) {
|
|
if (!FluidSystem::phaseIsActive(phaseIdx)) {
|
|
continue;
|
|
}
|
|
|
|
const unsigned activeCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::solventComponentIndex(phaseIdx));
|
|
mob[activeCompIdx] = extendEval(intQuants.mobility(phaseIdx));
|
|
}
|
|
if (has_solvent) {
|
|
mob[contiSolventEqIdx] = extendEval(intQuants.solventMobility());
|
|
}
|
|
} else {
|
|
|
|
const auto& paramsCell = materialLawManager->connectionMaterialLawParams(satid, cell_idx);
|
|
Eval relativePerms[3] = { 0.0, 0.0, 0.0 };
|
|
MaterialLaw::relativePermeabilities(relativePerms, paramsCell, intQuants.fluidState());
|
|
|
|
// reset the satnumvalue back to original
|
|
materialLawManager->connectionMaterialLawParams(satid_elem, cell_idx);
|
|
|
|
// compute the mobility
|
|
for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++phaseIdx) {
|
|
if (!FluidSystem::phaseIsActive(phaseIdx)) {
|
|
continue;
|
|
}
|
|
|
|
const unsigned activeCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::solventComponentIndex(phaseIdx));
|
|
mob[activeCompIdx] = extendEval(relativePerms[phaseIdx] / intQuants.fluidState().viscosity(phaseIdx));
|
|
}
|
|
|
|
// this may not work if viscosity and relperms has been modified?
|
|
if (has_solvent) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "individual mobility for wells does not work in combination with solvent", deferred_logger);
|
|
}
|
|
}
|
|
|
|
// modify the water mobility if polymer is present
|
|
if (has_polymer) {
|
|
if (!FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Water is required when polymer is active", deferred_logger);
|
|
}
|
|
|
|
updateWaterMobilityWithPolymer(ebosSimulator, perf, mob, deferred_logger);
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateWellState(const BVectorWell& dwells,
|
|
WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
if (!this->isOperable()) return;
|
|
|
|
updatePrimaryVariablesNewton(dwells, well_state);
|
|
|
|
updateWellStateFromPrimaryVariables(well_state, deferred_logger);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updatePrimaryVariablesNewton(const BVectorWell& dwells,
|
|
const WellState& /* well_state */) const
|
|
{
|
|
const double dFLimit = param_.dwell_fraction_max_;
|
|
|
|
const std::vector<double> old_primary_variables = primary_variables_;
|
|
|
|
// for injectors, very typical one of the fractions will be one, and it is easy to get zero value
|
|
// fractions. not sure what is the best way to handle it yet, so we just use 1.0 here
|
|
const double relaxation_factor_fractions = (well_type_ == PRODUCER) ?
|
|
relaxationFactorFractionsProducer(old_primary_variables, dwells)
|
|
: 1.0;
|
|
if (FluidSystem::numActivePhases() > 1) {
|
|
// update the second and third well variable (The flux fractions)
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
const int sign2 = dwells[0][WFrac] > 0 ? 1: -1;
|
|
const double dx2_limited = sign2 * std::min(std::abs(dwells[0][WFrac] * relaxation_factor_fractions), dFLimit);
|
|
// primary_variables_[WFrac] = old_primary_variables[WFrac] - dx2_limited;
|
|
primary_variables_[WFrac] = old_primary_variables[WFrac] - dx2_limited;
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
const int sign3 = dwells[0][GFrac] > 0 ? 1: -1;
|
|
const double dx3_limited = sign3 * std::min(std::abs(dwells[0][GFrac] * relaxation_factor_fractions), dFLimit);
|
|
primary_variables_[GFrac] = old_primary_variables[GFrac] - dx3_limited;
|
|
}
|
|
|
|
if (has_solvent) {
|
|
const int sign4 = dwells[0][SFrac] > 0 ? 1: -1;
|
|
const double dx4_limited = sign4 * std::min(std::abs(dwells[0][SFrac]) * relaxation_factor_fractions, dFLimit);
|
|
primary_variables_[SFrac] = old_primary_variables[SFrac] - dx4_limited;
|
|
}
|
|
|
|
processFractions();
|
|
}
|
|
|
|
// updating the total rates Q_t
|
|
const double relaxation_factor_rate = relaxationFactorRate(old_primary_variables, dwells);
|
|
primary_variables_[WQTotal] = old_primary_variables[WQTotal] - dwells[0][WQTotal] * relaxation_factor_rate;
|
|
|
|
// updating the bottom hole pressure
|
|
{
|
|
const double dBHPLimit = param_.dbhp_max_rel_;
|
|
const int sign1 = dwells[0][Bhp] > 0 ? 1: -1;
|
|
const double dx1_limited = sign1 * std::min(std::abs(dwells[0][Bhp]), std::abs(old_primary_variables[Bhp]) * dBHPLimit);
|
|
// 1e5 to make sure bhp will not be below 1bar
|
|
primary_variables_[Bhp] = std::max(old_primary_variables[Bhp] - dx1_limited, 1e5);
|
|
}
|
|
|
|
updateExtraPrimaryVariables(dwells);
|
|
|
|
for (double v : primary_variables_) {
|
|
assert(Opm::isfinite(v));
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateExtraPrimaryVariables(const BVectorWell& dwells) const
|
|
{
|
|
// for the water velocity and skin pressure
|
|
if (this->has_polymermw && well_type_ == INJECTOR) {
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
const int wat_vel_index = Bhp + 1 + perf;
|
|
const int pskin_index = Bhp + 1 + number_of_perforations_ + perf;
|
|
|
|
const double relaxation_factor = 0.9;
|
|
const double dx_wat_vel = dwells[0][wat_vel_index];
|
|
primary_variables_[wat_vel_index] -= relaxation_factor * dx_wat_vel;
|
|
|
|
const double dx_pskin = dwells[0][pskin_index];
|
|
primary_variables_[pskin_index] -= relaxation_factor * dx_pskin;
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
processFractions() const
|
|
{
|
|
assert(FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx));
|
|
const auto pu = phaseUsage();
|
|
std::vector<double> F(number_of_phases_, 0.0);
|
|
F[pu.phase_pos[Oil]] = 1.0;
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
F[pu.phase_pos[Water]] = primary_variables_[WFrac];
|
|
F[pu.phase_pos[Oil]] -= F[pu.phase_pos[Water]];
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
F[pu.phase_pos[Gas]] = primary_variables_[GFrac];
|
|
F[pu.phase_pos[Oil]] -= F[pu.phase_pos[Gas]];
|
|
}
|
|
|
|
double F_solvent = 0.0;
|
|
if (has_solvent) {
|
|
F_solvent = primary_variables_[SFrac];
|
|
F[pu.phase_pos[Oil]] -= F_solvent;
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
if (F[Water] < 0.0) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
F[pu.phase_pos[Gas]] /= (1.0 - F[pu.phase_pos[Water]]);
|
|
}
|
|
if (has_solvent) {
|
|
F_solvent /= (1.0 - F[pu.phase_pos[Water]]);
|
|
}
|
|
F[pu.phase_pos[Oil]] /= (1.0 - F[pu.phase_pos[Water]]);
|
|
F[pu.phase_pos[Water]] = 0.0;
|
|
}
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
if (F[pu.phase_pos[Gas]] < 0.0) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
F[pu.phase_pos[Water]] /= (1.0 - F[pu.phase_pos[Gas]]);
|
|
}
|
|
if (has_solvent) {
|
|
F_solvent /= (1.0 - F[pu.phase_pos[Gas]]);
|
|
}
|
|
F[pu.phase_pos[Oil]] /= (1.0 - F[pu.phase_pos[Gas]]);
|
|
F[pu.phase_pos[Gas]] = 0.0;
|
|
}
|
|
}
|
|
|
|
if (F[pu.phase_pos[Oil]] < 0.0) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
F[pu.phase_pos[Water]] /= (1.0 - F[pu.phase_pos[Oil]]);
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
F[pu.phase_pos[Gas]] /= (1.0 - F[pu.phase_pos[Oil]]);
|
|
}
|
|
if (has_solvent) {
|
|
F_solvent /= (1.0 - F[pu.phase_pos[Oil]]);
|
|
}
|
|
F[pu.phase_pos[Oil]] = 0.0;
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
primary_variables_[WFrac] = F[pu.phase_pos[Water]];
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
primary_variables_[GFrac] = F[pu.phase_pos[Gas]];
|
|
}
|
|
if(has_solvent) {
|
|
primary_variables_[SFrac] = F_solvent;
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateWellStateFromPrimaryVariables(WellState& well_state, Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
const PhaseUsage& pu = phaseUsage();
|
|
|
|
std::vector<double> F(number_of_phases_, 0.0);
|
|
if (FluidSystem::numActivePhases() == 1) {
|
|
F[0] = 1.0;
|
|
} else {
|
|
assert( FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) );
|
|
const int oil_pos = pu.phase_pos[Oil];
|
|
F[oil_pos] = 1.0;
|
|
|
|
if ( FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx) ) {
|
|
const int water_pos = pu.phase_pos[Water];
|
|
F[water_pos] = primary_variables_[WFrac];
|
|
F[oil_pos] -= F[water_pos];
|
|
}
|
|
|
|
if ( FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx) ) {
|
|
const int gas_pos = pu.phase_pos[Gas];
|
|
F[gas_pos] = primary_variables_[GFrac];
|
|
F[oil_pos] -= F[gas_pos];
|
|
}
|
|
|
|
double F_solvent = 0.0;
|
|
if (has_solvent) {
|
|
F_solvent = primary_variables_[SFrac];
|
|
F[oil_pos] -= F_solvent;
|
|
}
|
|
|
|
// convert the fractions to be Q_p / G_total to calculate the phase rates
|
|
for (int p = 0; p < number_of_phases_; ++p) {
|
|
const double scal = scalingFactor(p);
|
|
// for injection wells, there should only one non-zero scaling factor
|
|
if (scal > 0) {
|
|
F[p] /= scal ;
|
|
} else {
|
|
// this should only happens to injection wells
|
|
F[p] = 0.;
|
|
}
|
|
}
|
|
|
|
// F_solvent is added to F_gas. This means that well_rate[Gas] also contains solvent.
|
|
// More testing is needed to make sure this is correct for well groups and THP.
|
|
if (has_solvent){
|
|
F_solvent /= scalingFactor(contiSolventEqIdx);
|
|
F[pu.phase_pos[Gas]] += F_solvent;
|
|
}
|
|
|
|
}
|
|
well_state.bhp()[index_of_well_] = primary_variables_[Bhp];
|
|
|
|
// calculate the phase rates based on the primary variables
|
|
// for producers, this is not a problem, while not sure for injectors here
|
|
if (well_type_ == PRODUCER) {
|
|
const double g_total = primary_variables_[WQTotal];
|
|
for (int p = 0; p < number_of_phases_; ++p) {
|
|
well_state.wellRates()[index_of_well_ * number_of_phases_ + p] = g_total * F[p];
|
|
}
|
|
} else { // injectors
|
|
// TODO: using comp_frac_ here is very dangerous, since we do not update it based on the injection phase
|
|
// Either we use distr (might conflict with RESV related) or we update comp_frac_ based on the injection phase
|
|
for (int p = 0; p < number_of_phases_; ++p) {
|
|
const double comp_frac = comp_frac_[p];
|
|
well_state.wellRates()[index_of_well_ * number_of_phases_ + p] = comp_frac * primary_variables_[WQTotal];
|
|
}
|
|
}
|
|
|
|
updateThp(well_state, deferred_logger);
|
|
|
|
// other primary variables related to polymer injectivity study
|
|
if (this->has_polymermw && well_type_ == INJECTOR) {
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
well_state.perfWaterVelocity()[first_perf_ + perf] = primary_variables_[Bhp + 1 + perf];
|
|
well_state.perfSkinPressure()[first_perf_ + perf] = primary_variables_[Bhp + 1 + number_of_perforations_ + perf];
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateThp(WellState& well_state, Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
// When there is no vaild VFP table provided, we set the thp to be zero.
|
|
if (!this->isVFPActive(deferred_logger)) {
|
|
well_state.thp()[index_of_well_] = 0.;
|
|
return;
|
|
}
|
|
|
|
// avaiable VFP table is provided, we should update the thp value
|
|
|
|
// if the well is under THP control, we should use its target value
|
|
if (well_controls_get_current_type(well_controls_) == THP) {
|
|
well_state.thp()[index_of_well_] = well_controls_get_current_target(well_controls_);
|
|
} else {
|
|
// the well is under other control types, we calculate the thp based on bhp and rates
|
|
std::vector<double> rates(3, 0.0);
|
|
|
|
const Opm::PhaseUsage& pu = phaseUsage();
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
rates[ Water ] = well_state.wellRates()[index_of_well_ * number_of_phases_ + pu.phase_pos[ Water ] ];
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
rates[ Oil ] = well_state.wellRates()[index_of_well_ * number_of_phases_ + pu.phase_pos[ Oil ] ];
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
rates[ Gas ] = well_state.wellRates()[index_of_well_ * number_of_phases_ + pu.phase_pos[ Gas ] ];
|
|
}
|
|
|
|
const double bhp = well_state.bhp()[index_of_well_];
|
|
|
|
well_state.thp()[index_of_well_] = calculateThpFromBhp(rates, bhp, deferred_logger);
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateWellStateWithTarget(const Simulator& ebos_simulator,
|
|
WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
// number of phases
|
|
const int np = number_of_phases_;
|
|
const int well_index = index_of_well_;
|
|
const WellControls* wc = well_controls_;
|
|
const int current = well_state.currentControls()[well_index];
|
|
// Updating well state and primary variables.
|
|
// Target values are used as initial conditions for BHP, THP, and SURFACE_RATE
|
|
const double target = well_controls_iget_target(wc, current);
|
|
const double* distr = well_controls_iget_distr(wc, current);
|
|
switch (well_controls_iget_type(wc, current)) {
|
|
case BHP:
|
|
well_state.bhp()[well_index] = target;
|
|
// TODO: similar to the way below to handle THP
|
|
// we should not something related to thp here when there is thp constraint
|
|
// or when can calculate the THP (table avaiable or requested for output?)
|
|
// TODO: we should address this in a function updateWellStateWithBHPTarget.
|
|
// TODO: however, the reason that this one minght not be that critical with
|
|
// TODO: the effects remaining to be investigated.
|
|
break;
|
|
|
|
case THP: {
|
|
// when a well can not work under THP target, it switches to BHP control
|
|
if (this->operability_status_.isOperableUnderTHPLimit() ) {
|
|
updateWellStateWithTHPTargetIPR(ebos_simulator, well_state, deferred_logger);
|
|
} else { // go to BHP limit
|
|
assert(this->operability_status_.isOperableUnderBHPLimit() );
|
|
|
|
deferred_logger.info("well " + name() + " can not work with THP target, switching to BHP control");
|
|
|
|
well_state.bhp()[well_index] = mostStrictBhpFromBhpLimits(deferred_logger);
|
|
}
|
|
break;
|
|
}
|
|
|
|
case RESERVOIR_RATE: // intentional fall-through
|
|
case SURFACE_RATE:
|
|
// TODO: something needs to be done with BHP and THP here
|
|
// TODO: they should go to a separate function
|
|
// checking the number of the phases under control
|
|
int numPhasesWithTargetsUnderThisControl = 0;
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
if (distr[phase] > 0.0) {
|
|
numPhasesWithTargetsUnderThisControl += 1;
|
|
}
|
|
}
|
|
|
|
assert(numPhasesWithTargetsUnderThisControl > 0);
|
|
|
|
if (well_type_ == INJECTOR) {
|
|
// assign target value as initial guess for injectors
|
|
// only handles single phase control at the moment
|
|
assert(numPhasesWithTargetsUnderThisControl == 1);
|
|
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
if (distr[phase] > 0.) {
|
|
well_state.wellRates()[np*well_index + phase] = target / distr[phase];
|
|
} else {
|
|
well_state.wellRates()[np * well_index + phase] = 0.;
|
|
}
|
|
}
|
|
} else if (well_type_ == PRODUCER) {
|
|
// update the rates of phases under control based on the target,
|
|
// and also update rates of phases not under control to keep the rate ratio,
|
|
// assuming the mobility ratio does not change for the production wells
|
|
double original_rates_under_phase_control = 0.0;
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
if (distr[phase] > 0.0) {
|
|
original_rates_under_phase_control += well_state.wellRates()[np * well_index + phase] * distr[phase];
|
|
}
|
|
}
|
|
|
|
if (original_rates_under_phase_control != 0.0 ) {
|
|
const double scaling_factor = target / original_rates_under_phase_control;
|
|
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
well_state.wellRates()[np * well_index + phase] *= scaling_factor;
|
|
}
|
|
} else { // scaling factor is not well defined when original_rates_under_phase_control is zero
|
|
// separating targets equally between phases under control
|
|
const double target_rate_divided = target / numPhasesWithTargetsUnderThisControl;
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
if (distr[phase] > 0.0) {
|
|
well_state.wellRates()[np * well_index + phase] = target_rate_divided / distr[phase];
|
|
} else {
|
|
// this only happens for SURFACE_RATE control
|
|
well_state.wellRates()[np * well_index + phase] = target_rate_divided;
|
|
}
|
|
}
|
|
}
|
|
} else {
|
|
OPM_DEFLOG_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well", deferred_logger);
|
|
}
|
|
|
|
break;
|
|
} // end of switch
|
|
|
|
for (double v : primary_variables_) {
|
|
assert(Opm::isfinite(v));
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateIPR(const Simulator& ebos_simulator, Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
// TODO: not handling solvent related here for now
|
|
|
|
// TODO: it only handles the producers for now
|
|
// the formular for the injectors are not formulated yet
|
|
if (well_type_ == INJECTOR) {
|
|
return;
|
|
}
|
|
|
|
// initialize all the values to be zero to begin with
|
|
std::fill(ipr_a_.begin(), ipr_a_.end(), 0.);
|
|
std::fill(ipr_b_.begin(), ipr_b_.end(), 0.);
|
|
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
std::vector<EvalWell> mob(num_components_, {numWellEq_ + numEq, 0.0});
|
|
// TODO: mabye we should store the mobility somewhere, so that we only need to calculate it one per iteration
|
|
getMobility(ebos_simulator, perf, mob, deferred_logger);
|
|
|
|
const int cell_idx = well_cells_[perf];
|
|
const auto& int_quantities = *(ebos_simulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/ 0));
|
|
const auto& fs = int_quantities.fluidState();
|
|
// the pressure of the reservoir grid block the well connection is in
|
|
Eval perf_pressure = getPerfCellPressure(fs);
|
|
double p_r = perf_pressure.value();
|
|
|
|
// calculating the b for the connection
|
|
std::vector<double> b_perf(num_components_);
|
|
for (size_t phase = 0; phase < FluidSystem::numPhases; ++phase) {
|
|
if (!FluidSystem::phaseIsActive(phase)) {
|
|
continue;
|
|
}
|
|
const unsigned comp_idx = Indices::canonicalToActiveComponentIndex(FluidSystem::solventComponentIndex(phase));
|
|
b_perf[comp_idx] = fs.invB(phase).value();
|
|
}
|
|
|
|
// the pressure difference between the connection and BHP
|
|
const double h_perf = perf_pressure_diffs_[perf];
|
|
const double pressure_diff = p_r - h_perf;
|
|
|
|
// Let us add a check, since the pressure is calculated based on zero value BHP
|
|
// it should not be negative anyway. If it is negative, we might need to re-formulate
|
|
// to taking into consideration the crossflow here.
|
|
if (pressure_diff <= 0.) {
|
|
deferred_logger.warning("NON_POSITIVE_DRAWDOWN_IPR",
|
|
"non-positive drawdown found when updateIPR for well " + name());
|
|
}
|
|
|
|
// the well index associated with the connection
|
|
const double tw_perf = well_index_[perf]*ebos_simulator.problem().template rockCompTransMultiplier<double>(int_quantities, cell_idx);
|
|
|
|
// TODO: there might be some indices related problems here
|
|
// phases vs components
|
|
// ipr values for the perforation
|
|
std::vector<double> ipr_a_perf(ipr_a_.size());
|
|
std::vector<double> ipr_b_perf(ipr_b_.size());
|
|
for (int p = 0; p < number_of_phases_; ++p) {
|
|
const double tw_mob = tw_perf * mob[p].value() * b_perf[p];
|
|
ipr_a_perf[p] += tw_mob * pressure_diff;
|
|
ipr_b_perf[p] += tw_mob;
|
|
}
|
|
|
|
// we need to handle the rs and rv when both oil and gas are present
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) && FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
const unsigned oil_comp_idx = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
|
|
const unsigned gas_comp_idx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
|
|
const double rs = (fs.Rs()).value();
|
|
const double rv = (fs.Rv()).value();
|
|
|
|
const double dis_gas_a = rs * ipr_a_perf[oil_comp_idx];
|
|
const double vap_oil_a = rv * ipr_a_perf[gas_comp_idx];
|
|
|
|
ipr_a_perf[gas_comp_idx] += dis_gas_a;
|
|
ipr_a_perf[oil_comp_idx] += vap_oil_a;
|
|
|
|
const double dis_gas_b = rs * ipr_b_perf[oil_comp_idx];
|
|
const double vap_oil_b = rv * ipr_b_perf[gas_comp_idx];
|
|
|
|
ipr_b_perf[gas_comp_idx] += dis_gas_b;
|
|
ipr_b_perf[oil_comp_idx] += vap_oil_b;
|
|
}
|
|
|
|
for (int p = 0; p < number_of_phases_; ++p) {
|
|
// TODO: double check the indices here
|
|
ipr_a_[ebosCompIdxToFlowCompIdx(p)] += ipr_a_perf[p];
|
|
ipr_b_[ebosCompIdxToFlowCompIdx(p)] += ipr_b_perf[p];
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
checkWellOperability(const Simulator& ebos_simulator,
|
|
const WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
// focusing on PRODUCER for now
|
|
if (well_type_ == INJECTOR) {
|
|
return;
|
|
}
|
|
|
|
if (!this->underPredictionMode() ) {
|
|
return;
|
|
}
|
|
|
|
const bool old_well_operable = this->operability_status_.isOperable();
|
|
|
|
updateWellOperability(ebos_simulator, well_state, deferred_logger);
|
|
|
|
const bool well_operable = this->operability_status_.isOperable();
|
|
|
|
if (!well_operable && old_well_operable) {
|
|
deferred_logger.info(" well " + name() + " gets SHUT during iteration ");
|
|
} else if (well_operable && !old_well_operable) {
|
|
deferred_logger.info(" well " + name() + " gets REVIVED during iteration ");
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateWellOperability(const Simulator& ebos_simulator,
|
|
const WellState& /* well_state */,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
this->operability_status_.reset();
|
|
|
|
updateIPR(ebos_simulator, deferred_logger);
|
|
|
|
// checking the BHP limit related
|
|
checkOperabilityUnderBHPLimitProducer(ebos_simulator, deferred_logger);
|
|
|
|
// checking whether the well can operate under the THP constraints.
|
|
if (this->wellHasTHPConstraints()) {
|
|
checkOperabilityUnderTHPLimitProducer(ebos_simulator, deferred_logger);
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
checkOperabilityUnderBHPLimitProducer(const Simulator& ebos_simulator, Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
const double bhp_limit = mostStrictBhpFromBhpLimits(deferred_logger);
|
|
// Crude but works: default is one atmosphere.
|
|
// TODO: a better way to detect whether the BHP is defaulted or not
|
|
const bool bhp_limit_not_defaulted = bhp_limit > 1.5 * unit::barsa;
|
|
if ( bhp_limit_not_defaulted || !this->wellHasTHPConstraints() ) {
|
|
// if the BHP limit is not defaulted or the well does not have a THP limit
|
|
// we need to check the BHP limit
|
|
|
|
for (int p = 0; p < number_of_phases_; ++p) {
|
|
const double temp = ipr_a_[p] - ipr_b_[p] * bhp_limit;
|
|
if (temp < 0.) {
|
|
this->operability_status_.operable_under_only_bhp_limit = false;
|
|
break;
|
|
}
|
|
}
|
|
|
|
// checking whether running under BHP limit will violate THP limit
|
|
if (this->operability_status_.operable_under_only_bhp_limit && this->wellHasTHPConstraints()) {
|
|
// option 1: calculate well rates based on the BHP limit.
|
|
// option 2: stick with the above IPR curve
|
|
// we use IPR here
|
|
std::vector<double> well_rates_bhp_limit;
|
|
computeWellRatesWithBhp(ebos_simulator, bhp_limit, well_rates_bhp_limit, deferred_logger);
|
|
|
|
const double thp = calculateThpFromBhp(well_rates_bhp_limit, bhp_limit, deferred_logger);
|
|
const double thp_limit = this->getTHPConstraint(deferred_logger);
|
|
|
|
if (thp < thp_limit) {
|
|
this->operability_status_.obey_thp_limit_under_bhp_limit = false;
|
|
}
|
|
}
|
|
} else {
|
|
// defaulted BHP and there is a THP constraint
|
|
// default BHP limit is about 1 atm.
|
|
// when applied the hydrostatic pressure correction dp,
|
|
// most likely we get a negative value (bhp + dp)to search in the VFP table,
|
|
// which is not desirable.
|
|
// we assume we can operate under defaulted BHP limit and will violate the THP limit
|
|
// when operating under defaulted BHP limit.
|
|
this->operability_status_.operable_under_only_bhp_limit = true;
|
|
this->operability_status_.obey_thp_limit_under_bhp_limit = false;
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
checkOperabilityUnderTHPLimitProducer(const Simulator& /* ebos_simulator */, Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
const double obtain_bhp = calculateBHPWithTHPTargetIPR(deferred_logger);
|
|
|
|
if (obtain_bhp > 0.) {
|
|
this->operability_status_.can_obtain_bhp_with_thp_limit = true;
|
|
|
|
const double bhp_limit = mostStrictBhpFromBhpLimits(deferred_logger);
|
|
this->operability_status_.obey_bhp_limit_with_thp_limit = (obtain_bhp >= bhp_limit);
|
|
|
|
const double thp_limit = this->getTHPConstraint(deferred_logger);
|
|
if (obtain_bhp < thp_limit) {
|
|
const std::string msg = " obtained bhp " + std::to_string(unit::convert::to(obtain_bhp, unit::barsa))
|
|
+ " bars is SMALLER than thp limit "
|
|
+ std::to_string(unit::convert::to(thp_limit, unit::barsa))
|
|
+ " bars as a producer for well " + name();
|
|
deferred_logger.debug(msg);
|
|
}
|
|
} else {
|
|
this->operability_status_.can_obtain_bhp_with_thp_limit = false;
|
|
const double thp_limit = this->getTHPConstraint(deferred_logger);
|
|
deferred_logger.debug(" COULD NOT find bhp value under thp_limit "
|
|
+ std::to_string(unit::convert::to(thp_limit, unit::barsa))
|
|
+ " bars for well " + name() + ", the well might need to be closed ");
|
|
this->operability_status_.obey_bhp_limit_with_thp_limit = false;
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
bool
|
|
StandardWell<TypeTag>::
|
|
allDrawDownWrongDirection(const Simulator& ebos_simulator) const
|
|
{
|
|
bool all_drawdown_wrong_direction = true;
|
|
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
const int cell_idx = well_cells_[perf];
|
|
const auto& intQuants = *(ebos_simulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/0));
|
|
const auto& fs = intQuants.fluidState();
|
|
Eval perf_pressure = getPerfCellPressure(fs);
|
|
const double pressure = perf_pressure.value();
|
|
|
|
const double bhp = getBhp().value();
|
|
|
|
// Pressure drawdown (also used to determine direction of flow)
|
|
const double well_pressure = bhp + perf_pressure_diffs_[perf];
|
|
const double drawdown = pressure - well_pressure;
|
|
|
|
// for now, if there is one perforation can produce/inject in the correct
|
|
// direction, we consider this well can still produce/inject.
|
|
// TODO: it can be more complicated than this to cause wrong-signed rates
|
|
if ( (drawdown < 0. && well_type_ == INJECTOR) ||
|
|
(drawdown > 0. && well_type_ == PRODUCER) ) {
|
|
all_drawdown_wrong_direction = false;
|
|
break;
|
|
}
|
|
}
|
|
|
|
return all_drawdown_wrong_direction;
|
|
}
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
bool
|
|
StandardWell<TypeTag>::
|
|
canProduceInjectWithCurrentBhp(const Simulator& ebos_simulator,
|
|
const WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
const double bhp = well_state.bhp()[index_of_well_];
|
|
std::vector<double> well_rates;
|
|
computeWellRatesWithBhp(ebos_simulator, bhp, well_rates, deferred_logger);
|
|
|
|
const double sign = (well_type_ == PRODUCER) ? -1. : 1.;
|
|
const double threshold = sign * std::numeric_limits<double>::min();
|
|
|
|
bool can_produce_inject = false;
|
|
for (const auto value : well_rates) {
|
|
if (well_type_ == PRODUCER && value < threshold) {
|
|
can_produce_inject = true;
|
|
break;
|
|
} else if (well_type_ == INJECTOR && value > threshold) {
|
|
can_produce_inject = true;
|
|
break;
|
|
}
|
|
}
|
|
|
|
if (!can_produce_inject) {
|
|
deferred_logger.debug(" well " + name() + " CANNOT produce or inejct ");
|
|
}
|
|
|
|
return can_produce_inject;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
bool
|
|
StandardWell<TypeTag>::
|
|
openCrossFlowAvoidSingularity(const Simulator& ebos_simulator) const
|
|
{
|
|
return !getAllowCrossFlow() && allDrawDownWrongDirection(ebos_simulator);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateWellStateWithTHPTargetIPR(const Simulator& ebos_simulator,
|
|
WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
if (well_type_ == PRODUCER) {
|
|
updateWellStateWithTHPTargetIPRProducer(ebos_simulator,
|
|
well_state,
|
|
deferred_logger);
|
|
}
|
|
|
|
if (well_type_ == INJECTOR) {
|
|
well_state.thp()[index_of_well_] = this->getTHPConstraint(deferred_logger);
|
|
// TODO: more work needs to be done for the injectors here, while injectors
|
|
// have been okay with the current strategy relying on well control equation directly.
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateWellStateWithTHPTargetIPRProducer(const Simulator& ebos_simulator,
|
|
WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
|
|
well_state.thp()[index_of_well_] = this->getTHPConstraint(deferred_logger);
|
|
|
|
const double bhp = calculateBHPWithTHPTargetIPR(deferred_logger);
|
|
|
|
assert(bhp > 0.0);
|
|
|
|
well_state.bhp()[index_of_well_] = bhp;
|
|
|
|
// TODO: explicit quantities are always tricky for this type of situation
|
|
updatePrimaryVariables(well_state, deferred_logger);
|
|
initPrimaryVariablesEvaluation();
|
|
|
|
std::vector<double> rates;
|
|
computeWellRatesWithBhp(ebos_simulator, bhp, rates, deferred_logger);
|
|
|
|
// TODO: double checke the obtained rates
|
|
// this is another places we might obtain negative rates
|
|
|
|
for (int p = 0; p < number_of_phases_; ++p) {
|
|
well_state.wellRates()[number_of_phases_ * index_of_well_ + p] = rates[p];
|
|
}
|
|
|
|
// TODO: there will be something need to be done for the cases not the defaulted 3 phases,
|
|
// like 2 phases or solvent, polymer, etc. But we are not addressing them with THP control yet.
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
double
|
|
StandardWell<TypeTag>::
|
|
calculateBHPWithTHPTargetIPR(Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
const double thp_target = this->getTHPConstraint(deferred_logger);
|
|
const double thp_control_index = this->getControlIndex(THP);
|
|
const int thp_table_id = well_controls_iget_vfp(well_controls_, thp_control_index);
|
|
const double alq = well_controls_iget_alq(well_controls_, thp_control_index);
|
|
|
|
// not considering injectors for now
|
|
const double vfp_ref_depth = vfp_properties_->getProd()->getTable(thp_table_id)->getDatumDepth();
|
|
|
|
// the density of the top perforation
|
|
// TODO: make sure this is properly initialized
|
|
// TODO: with IPR, it should be possible, even this well is a new well, we do not have
|
|
// TODO: any information of previous rates. However, we are lacking the pressure though.
|
|
// TODO: but let us not do more work related now to see what will happen
|
|
const double rho = perf_densities_[0];
|
|
|
|
// TODO: call a/the function for dp
|
|
const double dp = (vfp_ref_depth - ref_depth_) * rho * gravity_;
|
|
|
|
const double bhp_limit = mostStrictBhpFromBhpLimits(deferred_logger);
|
|
|
|
const double obtain_bhp = vfp_properties_->getProd()->calculateBhpWithTHPTarget(ipr_a_, ipr_b_,
|
|
bhp_limit, thp_table_id, thp_target, alq, dp);
|
|
|
|
return obtain_bhp;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computePropertiesForWellConnectionPressures(const Simulator& ebosSimulator,
|
|
const WellState& well_state,
|
|
std::vector<double>& b_perf,
|
|
std::vector<double>& rsmax_perf,
|
|
std::vector<double>& rvmax_perf,
|
|
std::vector<double>& surf_dens_perf) const
|
|
{
|
|
const int nperf = number_of_perforations_;
|
|
const PhaseUsage& pu = phaseUsage();
|
|
b_perf.resize(nperf * num_components_);
|
|
surf_dens_perf.resize(nperf * num_components_);
|
|
const int w = index_of_well_;
|
|
|
|
const bool waterPresent = FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx);
|
|
const bool oilPresent = FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx);
|
|
const bool gasPresent = FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx);
|
|
|
|
//rs and rv are only used if both oil and gas is present
|
|
if (oilPresent && gasPresent) {
|
|
rsmax_perf.resize(nperf);
|
|
rvmax_perf.resize(nperf);
|
|
}
|
|
|
|
// Compute the average pressure in each well block
|
|
for (int perf = 0; perf < nperf; ++perf) {
|
|
const int cell_idx = well_cells_[perf];
|
|
const auto& intQuants = *(ebosSimulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/0));
|
|
const auto& fs = intQuants.fluidState();
|
|
|
|
// TODO: this is another place to show why WellState need to be a vector of WellState.
|
|
// TODO: to check why should be perf - 1
|
|
const double p_above = perf == 0 ? well_state.bhp()[w] : well_state.perfPress()[first_perf_ + perf - 1];
|
|
const double p_avg = (well_state.perfPress()[first_perf_ + perf] + p_above)/2;
|
|
// strange choice
|
|
const double temperature = fs.temperature(FluidSystem::oilPhaseIdx).value();
|
|
|
|
if (waterPresent) {
|
|
const unsigned waterCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx);
|
|
b_perf[ waterCompIdx + perf * num_components_] =
|
|
FluidSystem::waterPvt().inverseFormationVolumeFactor(fs.pvtRegionIndex(), temperature, p_avg);
|
|
}
|
|
|
|
if (gasPresent) {
|
|
const unsigned gasCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
|
|
const int gaspos = gasCompIdx + perf * num_components_;
|
|
const int gaspos_well = pu.phase_pos[Gas] + w * pu.num_phases;
|
|
|
|
if (oilPresent) {
|
|
const int oilpos_well = pu.phase_pos[Oil] + w * pu.num_phases;
|
|
const double oilrate = std::abs(well_state.wellRates()[oilpos_well]); //in order to handle negative rates in producers
|
|
rvmax_perf[perf] = FluidSystem::gasPvt().saturatedOilVaporizationFactor(fs.pvtRegionIndex(), temperature, p_avg);
|
|
if (oilrate > 0) {
|
|
const double gasrate = std::abs(well_state.wellRates()[gaspos_well]) - well_state.solventWellRate(w);
|
|
double rv = 0.0;
|
|
if (gasrate > 0) {
|
|
rv = oilrate / gasrate;
|
|
}
|
|
rv = std::min(rv, rvmax_perf[perf]);
|
|
|
|
b_perf[gaspos] = FluidSystem::gasPvt().inverseFormationVolumeFactor(fs.pvtRegionIndex(), temperature, p_avg, rv);
|
|
}
|
|
else {
|
|
b_perf[gaspos] = FluidSystem::gasPvt().saturatedInverseFormationVolumeFactor(fs.pvtRegionIndex(), temperature, p_avg);
|
|
}
|
|
|
|
} else {
|
|
b_perf[gaspos] = FluidSystem::gasPvt().saturatedInverseFormationVolumeFactor(fs.pvtRegionIndex(), temperature, p_avg);
|
|
}
|
|
}
|
|
|
|
if (oilPresent) {
|
|
const unsigned oilCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
|
|
const int oilpos = oilCompIdx + perf * num_components_;
|
|
const int oilpos_well = pu.phase_pos[Oil] + w * pu.num_phases;
|
|
if (gasPresent) {
|
|
rsmax_perf[perf] = FluidSystem::oilPvt().saturatedGasDissolutionFactor(fs.pvtRegionIndex(), temperature, p_avg);
|
|
const int gaspos_well = pu.phase_pos[Gas] + w * pu.num_phases;
|
|
const double gasrate = std::abs(well_state.wellRates()[gaspos_well]) - well_state.solventWellRate(w);
|
|
if (gasrate > 0) {
|
|
const double oilrate = std::abs(well_state.wellRates()[oilpos_well]);
|
|
double rs = 0.0;
|
|
if (oilrate > 0) {
|
|
rs = gasrate / oilrate;
|
|
}
|
|
rs = std::min(rs, rsmax_perf[perf]);
|
|
b_perf[oilpos] = FluidSystem::oilPvt().inverseFormationVolumeFactor(fs.pvtRegionIndex(), temperature, p_avg, rs);
|
|
} else {
|
|
b_perf[oilpos] = FluidSystem::oilPvt().saturatedInverseFormationVolumeFactor(fs.pvtRegionIndex(), temperature, p_avg);
|
|
}
|
|
} else {
|
|
b_perf[oilpos] = FluidSystem::oilPvt().saturatedInverseFormationVolumeFactor(fs.pvtRegionIndex(), temperature, p_avg);
|
|
}
|
|
}
|
|
|
|
// Surface density.
|
|
for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++phaseIdx) {
|
|
if (!FluidSystem::phaseIsActive(phaseIdx)) {
|
|
continue;
|
|
}
|
|
|
|
const unsigned compIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::solventComponentIndex(phaseIdx));
|
|
surf_dens_perf[num_components_ * perf + compIdx] = FluidSystem::referenceDensity( phaseIdx, fs.pvtRegionIndex() );
|
|
}
|
|
|
|
// We use cell values for solvent injector
|
|
if (has_solvent) {
|
|
b_perf[num_components_ * perf + contiSolventEqIdx] = intQuants.solventInverseFormationVolumeFactor().value();
|
|
surf_dens_perf[num_components_ * perf + contiSolventEqIdx] = intQuants.solventRefDensity();
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computeConnectionDensities(const std::vector<double>& perfComponentRates,
|
|
const std::vector<double>& b_perf,
|
|
const std::vector<double>& rsmax_perf,
|
|
const std::vector<double>& rvmax_perf,
|
|
const std::vector<double>& surf_dens_perf)
|
|
{
|
|
// Verify that we have consistent input.
|
|
const int np = number_of_phases_;
|
|
const int nperf = number_of_perforations_;
|
|
const int num_comp = num_components_;
|
|
|
|
// 1. Compute the flow (in surface volume units for each
|
|
// component) exiting up the wellbore from each perforation,
|
|
// taking into account flow from lower in the well, and
|
|
// in/out-flow at each perforation.
|
|
std::vector<double> q_out_perf(nperf*num_comp);
|
|
|
|
// TODO: investigate whether we should use the following techniques to calcuate the composition of flows in the wellbore
|
|
// Iterate over well perforations from bottom to top.
|
|
for (int perf = nperf - 1; perf >= 0; --perf) {
|
|
for (int component = 0; component < num_comp; ++component) {
|
|
if (perf == nperf - 1) {
|
|
// This is the bottom perforation. No flow from below.
|
|
q_out_perf[perf*num_comp+ component] = 0.0;
|
|
} else {
|
|
// Set equal to flow from below.
|
|
q_out_perf[perf*num_comp + component] = q_out_perf[(perf+1)*num_comp + component];
|
|
}
|
|
// Subtract outflow through perforation.
|
|
q_out_perf[perf*num_comp + component] -= perfComponentRates[perf*num_comp + component];
|
|
}
|
|
}
|
|
|
|
// 2. Compute the component mix at each perforation as the
|
|
// absolute values of the surface rates divided by their sum.
|
|
// Then compute volume ratios (formation factors) for each perforation.
|
|
// Finally compute densities for the segments associated with each perforation.
|
|
std::vector<double> mix(num_comp,0.0);
|
|
std::vector<double> x(num_comp);
|
|
std::vector<double> surf_dens(num_comp);
|
|
|
|
for (int perf = 0; perf < nperf; ++perf) {
|
|
// Find component mix.
|
|
const double tot_surf_rate = std::accumulate(q_out_perf.begin() + num_comp*perf,
|
|
q_out_perf.begin() + num_comp*(perf+1), 0.0);
|
|
if (tot_surf_rate != 0.0) {
|
|
for (int component = 0; component < num_comp; ++component) {
|
|
mix[component] = std::fabs(q_out_perf[perf*num_comp + component]/tot_surf_rate);
|
|
}
|
|
} else {
|
|
// No flow => use well specified fractions for mix.
|
|
for (int component = 0; component < num_comp; ++component) {
|
|
if (component < np) {
|
|
mix[component] = comp_frac_[ ebosCompIdxToFlowCompIdx(component)];
|
|
}
|
|
}
|
|
// intialize 0.0 for comIdx >= np;
|
|
}
|
|
// Compute volume ratio.
|
|
x = mix;
|
|
|
|
// Subtract dissolved gas from oil phase and vapporized oil from gas phase
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasCompIdx) && FluidSystem::phaseIsActive(FluidSystem::oilCompIdx)) {
|
|
const unsigned gaspos = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
|
|
const unsigned oilpos = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
|
|
double rs = 0.0;
|
|
double rv = 0.0;
|
|
if (!rsmax_perf.empty() && mix[oilpos] > 0.0) {
|
|
rs = std::min(mix[gaspos]/mix[oilpos], rsmax_perf[perf]);
|
|
}
|
|
if (!rvmax_perf.empty() && mix[gaspos] > 0.0) {
|
|
rv = std::min(mix[oilpos]/mix[gaspos], rvmax_perf[perf]);
|
|
}
|
|
if (rs != 0.0) {
|
|
// Subtract gas in oil from gas mixture
|
|
x[gaspos] = (mix[gaspos] - mix[oilpos]*rs)/(1.0 - rs*rv);
|
|
}
|
|
if (rv != 0.0) {
|
|
// Subtract oil in gas from oil mixture
|
|
x[oilpos] = (mix[oilpos] - mix[gaspos]*rv)/(1.0 - rs*rv);;
|
|
}
|
|
}
|
|
double volrat = 0.0;
|
|
for (int component = 0; component < num_comp; ++component) {
|
|
volrat += x[component] / b_perf[perf*num_comp+ component];
|
|
}
|
|
for (int component = 0; component < num_comp; ++component) {
|
|
surf_dens[component] = surf_dens_perf[perf*num_comp+ component];
|
|
}
|
|
|
|
// Compute segment density.
|
|
perf_densities_[perf] = std::inner_product(surf_dens.begin(), surf_dens.end(), mix.begin(), 0.0) / volrat;
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computeConnectionPressureDelta()
|
|
{
|
|
// Algorithm:
|
|
|
|
// We'll assume the perforations are given in order from top to
|
|
// bottom for each well. By top and bottom we do not necessarily
|
|
// mean in a geometric sense (depth), but in a topological sense:
|
|
// the 'top' perforation is nearest to the surface topologically.
|
|
// Our goal is to compute a pressure delta for each perforation.
|
|
|
|
// 1. Compute pressure differences between perforations.
|
|
// dp_perf will contain the pressure difference between a
|
|
// perforation and the one above it, except for the first
|
|
// perforation for each well, for which it will be the
|
|
// difference to the reference (bhp) depth.
|
|
|
|
const int nperf = number_of_perforations_;
|
|
perf_pressure_diffs_.resize(nperf, 0.0);
|
|
|
|
for (int perf = 0; perf < nperf; ++perf) {
|
|
const double z_above = perf == 0 ? ref_depth_ : perf_depth_[perf - 1];
|
|
const double dz = perf_depth_[perf] - z_above;
|
|
perf_pressure_diffs_[perf] = dz * perf_densities_[perf] * gravity_;
|
|
}
|
|
|
|
// 2. Compute pressure differences to the reference point (bhp) by
|
|
// accumulating the already computed adjacent pressure
|
|
// differences, storing the result in dp_perf.
|
|
// This accumulation must be done per well.
|
|
const auto beg = perf_pressure_diffs_.begin();
|
|
const auto end = perf_pressure_diffs_.end();
|
|
std::partial_sum(beg, end, beg);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
ConvergenceReport
|
|
StandardWell<TypeTag>::
|
|
getWellConvergence(const std::vector<double>& B_avg,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
// the following implementation assume that the polymer is always after the w-o-g phases
|
|
// For the polymer, energy and foam cases, there is one more mass balance equations of reservoir than wells
|
|
assert((int(B_avg.size()) == num_components_) || has_polymer || has_energy || has_foam);
|
|
|
|
const double tol_wells = param_.tolerance_wells_;
|
|
const double maxResidualAllowed = param_.max_residual_allowed_;
|
|
|
|
std::vector<double> res(numWellEq_);
|
|
for (int eq_idx = 0; eq_idx < numWellEq_; ++eq_idx) {
|
|
// magnitude of the residual matters
|
|
res[eq_idx] = std::abs(resWell_[0][eq_idx]);
|
|
}
|
|
|
|
std::vector<double> well_flux_residual(num_components_);
|
|
|
|
// Finish computation
|
|
for ( int compIdx = 0; compIdx < num_components_; ++compIdx )
|
|
{
|
|
well_flux_residual[compIdx] = B_avg[compIdx] * res[compIdx];
|
|
}
|
|
|
|
ConvergenceReport report;
|
|
using CR = ConvergenceReport;
|
|
CR::WellFailure::Type type = CR::WellFailure::Type::MassBalance;
|
|
// checking if any NaN or too large residuals found
|
|
for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++phaseIdx) {
|
|
if (!FluidSystem::phaseIsActive(phaseIdx)) {
|
|
continue;
|
|
}
|
|
|
|
const unsigned canonicalCompIdx = FluidSystem::solventComponentIndex(phaseIdx);
|
|
const int compIdx = Indices::canonicalToActiveComponentIndex(canonicalCompIdx);
|
|
|
|
if (std::isnan(well_flux_residual[compIdx])) {
|
|
report.setWellFailed({type, CR::Severity::NotANumber, compIdx, name()});
|
|
} else if (well_flux_residual[compIdx] > maxResidualAllowed) {
|
|
report.setWellFailed({type, CR::Severity::TooLarge, compIdx, name()});
|
|
} else if (well_flux_residual[compIdx] > tol_wells) {
|
|
report.setWellFailed({type, CR::Severity::Normal, compIdx, name()});
|
|
}
|
|
}
|
|
|
|
checkConvergenceControlEq(report, deferred_logger);
|
|
|
|
checkConvergenceExtraEqs(res, report);
|
|
|
|
return report;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computeWellConnectionDensitesPressures(const WellState& well_state,
|
|
const std::vector<double>& b_perf,
|
|
const std::vector<double>& rsmax_perf,
|
|
const std::vector<double>& rvmax_perf,
|
|
const std::vector<double>& surf_dens_perf)
|
|
{
|
|
// Compute densities
|
|
const int nperf = number_of_perforations_;
|
|
const int np = number_of_phases_;
|
|
std::vector<double> perfRates(b_perf.size(),0.0);
|
|
|
|
for (int perf = 0; perf < nperf; ++perf) {
|
|
for (int comp = 0; comp < np; ++comp) {
|
|
perfRates[perf * num_components_ + comp] = well_state.perfPhaseRates()[(first_perf_ + perf) * np + ebosCompIdxToFlowCompIdx(comp)];
|
|
}
|
|
if(has_solvent) {
|
|
perfRates[perf * num_components_ + contiSolventEqIdx] = well_state.perfRateSolvent()[first_perf_ + perf];
|
|
}
|
|
}
|
|
|
|
computeConnectionDensities(perfRates, b_perf, rsmax_perf, rvmax_perf, surf_dens_perf);
|
|
|
|
computeConnectionPressureDelta();
|
|
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computeWellConnectionPressures(const Simulator& ebosSimulator,
|
|
const WellState& well_state)
|
|
{
|
|
// 1. Compute properties required by computeConnectionPressureDelta().
|
|
// Note that some of the complexity of this part is due to the function
|
|
// taking std::vector<double> arguments, and not Eigen objects.
|
|
std::vector<double> b_perf;
|
|
std::vector<double> rsmax_perf;
|
|
std::vector<double> rvmax_perf;
|
|
std::vector<double> surf_dens_perf;
|
|
computePropertiesForWellConnectionPressures(ebosSimulator, well_state, b_perf, rsmax_perf, rvmax_perf, surf_dens_perf);
|
|
computeWellConnectionDensitesPressures(well_state, b_perf, rsmax_perf, rvmax_perf, surf_dens_perf);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
solveEqAndUpdateWellState(WellState& well_state, Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
if (!this->isOperable()) return;
|
|
|
|
// We assemble the well equations, then we check the convergence,
|
|
// which is why we do not put the assembleWellEq here.
|
|
BVectorWell dx_well(1);
|
|
dx_well[0].resize(numWellEq_);
|
|
invDuneD_.mv(resWell_, dx_well);
|
|
|
|
updateWellState(dx_well, well_state, deferred_logger);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
calculateExplicitQuantities(const Simulator& ebosSimulator,
|
|
const WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
updatePrimaryVariables(well_state, deferred_logger);
|
|
initPrimaryVariablesEvaluation();
|
|
computeWellConnectionPressures(ebosSimulator, well_state);
|
|
computeAccumWell();
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computeAccumWell()
|
|
{
|
|
for (int eq_idx = 0; eq_idx < numWellConservationEq; ++eq_idx) {
|
|
F0_[eq_idx] = wellSurfaceVolumeFraction(eq_idx).value();
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
apply(const BVector& x, BVector& Ax) const
|
|
{
|
|
if (!this->isOperable()) return;
|
|
|
|
if ( param_.matrix_add_well_contributions_ )
|
|
{
|
|
// Contributions are already in the matrix itself
|
|
return;
|
|
}
|
|
assert( Bx_.size() == duneB_.N() );
|
|
assert( invDrw_.size() == invDuneD_.N() );
|
|
|
|
// Bx_ = duneB_ * x
|
|
duneB_.mv(x, Bx_);
|
|
// invDBx = invDuneD_ * Bx_
|
|
// TODO: with this, we modified the content of the invDrw_.
|
|
// Is it necessary to do this to save some memory?
|
|
BVectorWell& invDBx = invDrw_;
|
|
invDuneD_.mv(Bx_, invDBx);
|
|
|
|
// Ax = Ax - duneC_^T * invDBx
|
|
duneC_.mmtv(invDBx,Ax);
|
|
}
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
apply(BVector& r) const
|
|
{
|
|
if (!this->isOperable()) return;
|
|
|
|
assert( invDrw_.size() == invDuneD_.N() );
|
|
|
|
// invDrw_ = invDuneD_ * resWell_
|
|
invDuneD_.mv(resWell_, invDrw_);
|
|
// r = r - duneC_^T * invDrw_
|
|
duneC_.mmtv(invDrw_, r);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
recoverSolutionWell(const BVector& x, BVectorWell& xw) const
|
|
{
|
|
if (!this->isOperable()) return;
|
|
|
|
BVectorWell resWell = resWell_;
|
|
// resWell = resWell - B * x
|
|
duneB_.mmv(x, resWell);
|
|
// xw = D^-1 * resWell
|
|
invDuneD_.mv(resWell, xw);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
recoverWellSolutionAndUpdateWellState(const BVector& x,
|
|
WellState& well_state,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
if (!this->isOperable()) return;
|
|
|
|
BVectorWell xw(1);
|
|
xw[0].resize(numWellEq_);
|
|
|
|
recoverSolutionWell(x, xw);
|
|
updateWellState(xw, well_state, deferred_logger);
|
|
}
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computeWellRatesWithBhp(const Simulator& ebosSimulator,
|
|
const double& bhp,
|
|
std::vector<double>& well_flux,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
|
|
const int np = number_of_phases_;
|
|
well_flux.resize(np, 0.0);
|
|
|
|
const bool allow_cf = getAllowCrossFlow();
|
|
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
const int cell_idx = well_cells_[perf];
|
|
const auto& intQuants = *(ebosSimulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/ 0));
|
|
// flux for each perforation
|
|
std::vector<EvalWell> mob(num_components_, {numWellEq_ + numEq, 0.});
|
|
getMobility(ebosSimulator, perf, mob, deferred_logger);
|
|
double trans_mult = ebosSimulator.problem().template rockCompTransMultiplier<double>(intQuants, cell_idx);
|
|
const double Tw = well_index_[perf] * trans_mult;
|
|
|
|
std::vector<EvalWell> cq_s(num_components_, {numWellEq_ + numEq, 0.});
|
|
double perf_dis_gas_rate = 0.;
|
|
double perf_vap_oil_rate = 0.;
|
|
computePerfRate(intQuants, mob, EvalWell(numWellEq_ + numEq, bhp), Tw, perf, allow_cf,
|
|
cq_s, perf_dis_gas_rate, perf_vap_oil_rate, deferred_logger);
|
|
|
|
for(int p = 0; p < np; ++p) {
|
|
well_flux[ebosCompIdxToFlowCompIdx(p)] += cq_s[p].value();
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computeWellRatesWithBhpPotential(const Simulator& ebosSimulator,
|
|
const std::vector<Scalar>& B_avg,
|
|
const double& bhp,
|
|
std::vector<double>& well_flux,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
|
|
WellControls* wc = well_controls_;
|
|
const int bhp_index = Base::getControlIndex(BHP);
|
|
const double orig_bhp = well_controls_iget_target(wc, bhp_index);
|
|
const auto orig_current = well_controls_get_current(wc);
|
|
|
|
well_controls_iset_target(wc, bhp_index, bhp);
|
|
well_controls_set_current(wc, bhp_index);
|
|
|
|
// iterate to get a more accurate well density
|
|
// create a copy of the well_state to use. If the operability checking is sucessful, we use this one
|
|
// to replace the original one
|
|
WellState well_state_copy = ebosSimulator.problem().wellModel().wellState();
|
|
well_state_copy.currentControls()[index_of_well_] = bhp_index;
|
|
|
|
bool converged = this->solveWellEqUntilConverged(ebosSimulator, B_avg, well_state_copy, deferred_logger);
|
|
|
|
if (!converged) {
|
|
const std::string msg = " well " + name() + " did not get converged during well potential calculations "
|
|
"returning zero values for the potential";
|
|
deferred_logger.debug(msg);
|
|
return;
|
|
}
|
|
updatePrimaryVariables(well_state_copy, deferred_logger);
|
|
computeWellConnectionPressures(ebosSimulator, well_state_copy);
|
|
initPrimaryVariablesEvaluation();
|
|
|
|
|
|
computeWellRatesWithBhp(ebosSimulator, bhp, well_flux, deferred_logger);
|
|
|
|
// reset bhp limit
|
|
well_controls_iset_target(wc, bhp_index, orig_bhp);
|
|
well_controls_set_current(wc, orig_current);
|
|
}
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
std::vector<double>
|
|
StandardWell<TypeTag>::
|
|
computeWellPotentialWithTHP(const Simulator& ebosSimulator,
|
|
const std::vector<Scalar>& B_avg,
|
|
const double initial_bhp, // bhp from BHP constraints
|
|
const std::vector<double>& initial_potential,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
// TODO: pay attention to the situation that finally the potential is calculated based on the bhp control
|
|
// TODO: should we consider the bhp constraints during the iterative process?
|
|
const int np = number_of_phases_;
|
|
|
|
assert( np == int(initial_potential.size()) );
|
|
|
|
std::vector<double> potentials = initial_potential;
|
|
std::vector<double> old_potentials = potentials; // keeping track of the old potentials
|
|
|
|
double bhp = initial_bhp;
|
|
double old_bhp = bhp;
|
|
|
|
bool converged = false;
|
|
const int max_iteration = 1000;
|
|
const double bhp_tolerance = 1000.; // 1000 pascal
|
|
|
|
int iteration = 0;
|
|
|
|
while ( !converged && iteration < max_iteration ) {
|
|
// for each iteration, we calculate the bhp based on the rates/potentials with thp constraints
|
|
// with considering the bhp value from the bhp limits. At the beginning of each iteration,
|
|
// we initialize the bhp to be the bhp value from the bhp limits. Then based on the bhp values calculated
|
|
// from the thp constraints, we decide the effective bhp value for well potential calculation.
|
|
bhp = initial_bhp;
|
|
|
|
// The number of the well controls/constraints
|
|
const int nwc = well_controls_get_num(well_controls_);
|
|
|
|
for (int ctrl_index = 0; ctrl_index < nwc; ++ctrl_index) {
|
|
if (well_controls_iget_type(well_controls_, ctrl_index) == THP) {
|
|
const Opm::PhaseUsage& pu = phaseUsage();
|
|
|
|
std::vector<double> rates(3, 0.0);
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
rates[ Water ] = potentials[pu.phase_pos[ Water ] ];
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
rates[ Oil ] = potentials[pu.phase_pos[ Oil ] ];
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
rates[ Gas ] = potentials[pu.phase_pos[ Gas ] ];
|
|
}
|
|
|
|
const double bhp_calculated = calculateBhpFromThp(rates, ctrl_index, deferred_logger);
|
|
|
|
if (well_type_ == INJECTOR && bhp_calculated < bhp ) {
|
|
bhp = bhp_calculated;
|
|
}
|
|
|
|
if (well_type_ == PRODUCER && bhp_calculated > bhp) {
|
|
bhp = bhp_calculated;
|
|
}
|
|
}
|
|
}
|
|
|
|
// there should be always some available bhp/thp constraints there
|
|
if (std::isinf(bhp) || std::isnan(bhp)) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Unvalid bhp value obtained during the potential calculation for well " << name(), deferred_logger);
|
|
}
|
|
|
|
converged = std::abs(old_bhp - bhp) < bhp_tolerance;
|
|
|
|
computeWellRatesWithBhpPotential(ebosSimulator, B_avg, bhp, potentials, deferred_logger);
|
|
|
|
// checking whether the potentials have valid values
|
|
for (const double value : potentials) {
|
|
if (std::isinf(value) || std::isnan(value)) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Unvalid potential value obtained during the potential calculation for well " << name(), deferred_logger);
|
|
}
|
|
}
|
|
|
|
if (!converged) {
|
|
old_bhp = bhp;
|
|
for (int p = 0; p < np; ++p) {
|
|
// TODO: improve the interpolation, will it always be valid with the way below?
|
|
// TODO: finding better paramters, better iteration strategy for better convergence rate.
|
|
const double potential_update_damping_factor = 0.001;
|
|
potentials[p] = potential_update_damping_factor * potentials[p] + (1.0 - potential_update_damping_factor) * old_potentials[p];
|
|
old_potentials[p] = potentials[p];
|
|
}
|
|
}
|
|
|
|
++iteration;
|
|
}
|
|
|
|
if (!converged) {
|
|
// TODO: temporary approach to recover the running of prediction case
|
|
// more sophisicated treatment should be developed to handle the situation in a general way
|
|
// OPM_DEFLOG_THROW(std::runtime_error, "Failed in getting converged for the potential calculation for well " << name(), deferred_logger);
|
|
deferred_logger.warning("FAILURE_GETTING_CONVERGED_POTENTIAL",
|
|
"Failed in getting converged for the potential calculation for well " + name());
|
|
}
|
|
|
|
return potentials;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
computeWellPotentials(const Simulator& ebosSimulator,
|
|
const std::vector<Scalar>& B_avg,
|
|
const WellState& well_state,
|
|
std::vector<double>& well_potentials,
|
|
Opm::DeferredLogger& deferred_logger) // const
|
|
{
|
|
|
|
// creating a copy of the well itself, to avoid messing up the explicit informations
|
|
// during this copy, the only information not copied properly is the well controls
|
|
StandardWell<TypeTag> well(*this);
|
|
|
|
well.well_controls_ = this->createWellControlsWithBHPAndTHP(deferred_logger);
|
|
|
|
well.updatePrimaryVariables(well_state, deferred_logger);
|
|
well.computeWellConnectionPressures(ebosSimulator, well_state);
|
|
|
|
// initialize the primary variables in Evaluation, which is used in computePerfRate for computeWellPotentials
|
|
// TODO: for computeWellPotentials, no derivative is required actually
|
|
well.initPrimaryVariablesEvaluation();
|
|
|
|
const int np = number_of_phases_;
|
|
well_potentials.resize(np, 0.0);
|
|
|
|
// get the bhp value based on the bhp constraints
|
|
const double bhp = well.mostStrictBhpFromBhpLimits(deferred_logger);
|
|
|
|
// does the well have a THP related constraint?
|
|
if ( !well.wellHasTHPConstraints() ) {
|
|
assert(std::abs(bhp) != std::numeric_limits<double>::max());
|
|
well.computeWellRatesWithBhpPotential(ebosSimulator, B_avg, bhp, well_potentials, deferred_logger);
|
|
} else {
|
|
// the well has a THP related constraint
|
|
// checking whether a well is newly added, it only happens at the beginning of the report step
|
|
if ( !well_state.effectiveEventsOccurred(index_of_well_) ) {
|
|
for (int p = 0; p < np; ++p) {
|
|
// This is dangerous for new added well
|
|
// since we are not handling the initialization correctly for now
|
|
well_potentials[p] = well_state.wellRates()[index_of_well_ * np + p];
|
|
}
|
|
} else {
|
|
// We need to generate a reasonable rates to start the iteration process
|
|
well.computeWellRatesWithBhpPotential(ebosSimulator, B_avg, bhp, well_potentials, deferred_logger);
|
|
for (double& value : well_potentials) {
|
|
// make the value a little safer in case the BHP limits are default ones
|
|
// TODO: a better way should be a better rescaling based on the investigation of the VFP table.
|
|
const double rate_safety_scaling_factor = 0.00001;
|
|
value *= rate_safety_scaling_factor;
|
|
}
|
|
}
|
|
|
|
well_potentials = well.computeWellPotentialWithTHP(ebosSimulator, B_avg, bhp, well_potentials, deferred_logger);
|
|
}
|
|
|
|
|
|
// destroy the newly created WellControls
|
|
well_controls_destroy(well.well_controls_);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updatePrimaryVariables(const WellState& well_state, Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
if (!this->isOperable()) return;
|
|
|
|
const int well_index = index_of_well_;
|
|
const int np = number_of_phases_;
|
|
|
|
// the weighted total well rate
|
|
double total_well_rate = 0.0;
|
|
for (int p = 0; p < np; ++p) {
|
|
total_well_rate += scalingFactor(p) * well_state.wellRates()[np * well_index + p];
|
|
}
|
|
|
|
// Not: for the moment, the first primary variable for the injectors is not G_total. The injection rate
|
|
// under surface condition is used here
|
|
if (well_type_ == INJECTOR) {
|
|
primary_variables_[WQTotal] = 0.;
|
|
for (int p = 0; p < np; ++p) {
|
|
// TODO: the use of comp_frac_ here is dangerous, since the injection phase can be different from
|
|
// prefered phasse in WELSPECS, while comp_frac_ only reflect the one specified in WELSPECS
|
|
primary_variables_[WQTotal] += well_state.wellRates()[np * well_index + p] * comp_frac_[p];
|
|
}
|
|
} else {
|
|
for (int p = 0; p < np; ++p) {
|
|
primary_variables_[WQTotal] = total_well_rate;
|
|
}
|
|
}
|
|
|
|
if (FluidSystem::numActivePhases() > 1) {
|
|
if (std::abs(total_well_rate) > 0.) {
|
|
const auto pu = phaseUsage();
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
primary_variables_[WFrac] = scalingFactor(pu.phase_pos[Water]) * well_state.wellRates()[np*well_index + pu.phase_pos[Water]] / total_well_rate;
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
primary_variables_[GFrac] = scalingFactor(pu.phase_pos[Gas]) * (well_state.wellRates()[np*well_index + pu.phase_pos[Gas]] - well_state.solventWellRate(well_index)) / total_well_rate ;
|
|
}
|
|
if (has_solvent) {
|
|
primary_variables_[SFrac] = scalingFactor(pu.phase_pos[Gas]) * well_state.solventWellRate(well_index) / total_well_rate ;
|
|
}
|
|
} else { // total_well_rate == 0
|
|
if (well_type_ == INJECTOR) {
|
|
auto phase = well_ecl_.getInjectionProperties().injectorType;
|
|
// only single phase injection handled
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
if (phase == Well2::InjectorType::WATER) {
|
|
primary_variables_[WFrac] = 1.0;
|
|
} else {
|
|
primary_variables_[WFrac] = 0.0;
|
|
}
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
if (phase == Well2::InjectorType::GAS) {
|
|
primary_variables_[GFrac] = 1.0 - wsolvent();
|
|
if (has_solvent) {
|
|
primary_variables_[SFrac] = wsolvent();
|
|
}
|
|
} else {
|
|
primary_variables_[GFrac] = 0.0;
|
|
}
|
|
}
|
|
|
|
// TODO: it is possible to leave injector as a oil well,
|
|
// when F_w and F_g both equals to zero, not sure under what kind of circumstance
|
|
// this will happen.
|
|
} else if (well_type_ == PRODUCER) { // producers
|
|
// TODO: the following are not addressed for the solvent case yet
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
primary_variables_[WFrac] = 1.0 / np;
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
primary_variables_[GFrac] = 1.0 / np;
|
|
}
|
|
} else {
|
|
OPM_DEFLOG_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well", deferred_logger);
|
|
}
|
|
}
|
|
}
|
|
|
|
// BHP
|
|
primary_variables_[Bhp] = well_state.bhp()[index_of_well_];
|
|
|
|
// other primary variables related to polymer injection
|
|
if (this->has_polymermw && well_type_ == INJECTOR) {
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
primary_variables_[Bhp + 1 + perf] = well_state.perfWaterVelocity()[first_perf_ + perf];
|
|
primary_variables_[Bhp + 1 + number_of_perforations_ + perf] = well_state.perfSkinPressure()[first_perf_ + perf];
|
|
}
|
|
}
|
|
|
|
for (double v : primary_variables_) {
|
|
assert(Opm::isfinite(v));
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
template<class ValueType>
|
|
ValueType
|
|
StandardWell<TypeTag>::
|
|
calculateBhpFromThp(const std::vector<ValueType>& rates,
|
|
const int control_index,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
// TODO: when well is under THP control, the BHP is dependent on the rates,
|
|
// the well rates is also dependent on the BHP, so it might need to do some iteration.
|
|
// However, when group control is involved, change of the rates might impacts other wells
|
|
// so iterations on a higher level will be required. Some investigation might be needed when
|
|
// we face problems under THP control.
|
|
|
|
assert(int(rates.size()) == 3); // the vfp related only supports three phases now.
|
|
|
|
const ValueType aqua = rates[Water];
|
|
const ValueType liquid = rates[Oil];
|
|
const ValueType vapour = rates[Gas];
|
|
|
|
const int vfp = well_controls_iget_vfp(well_controls_, control_index);
|
|
const double& thp = well_controls_iget_target(well_controls_, control_index);
|
|
const double& alq = well_controls_iget_alq(well_controls_, control_index);
|
|
|
|
// pick the density in the top layer
|
|
// TODO: it is possible it should be a Evaluation
|
|
const double rho = perf_densities_[0];
|
|
|
|
if (well_type_ == INJECTOR) {
|
|
const double vfp_ref_depth = vfp_properties_->getInj()->getTable(vfp)->getDatumDepth();
|
|
|
|
const double dp = wellhelpers::computeHydrostaticCorrection(ref_depth_, vfp_ref_depth, rho, gravity_);
|
|
|
|
return vfp_properties_->getInj()->bhp(vfp, aqua, liquid, vapour, thp) - dp;
|
|
}
|
|
else if (well_type_ == PRODUCER) {
|
|
const double vfp_ref_depth = vfp_properties_->getProd()->getTable(vfp)->getDatumDepth();
|
|
|
|
const double dp = wellhelpers::computeHydrostaticCorrection(ref_depth_, vfp_ref_depth, rho, gravity_);
|
|
|
|
return vfp_properties_->getProd()->bhp(vfp, aqua, liquid, vapour, thp, alq) - dp;
|
|
}
|
|
else {
|
|
OPM_DEFLOG_THROW(std::logic_error, "Expected INJECTOR or PRODUCER well", deferred_logger);
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
double
|
|
StandardWell<TypeTag>::
|
|
calculateThpFromBhp(const std::vector<double>& rates,
|
|
const double bhp,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
assert(int(rates.size()) == 3); // the vfp related only supports three phases now.
|
|
|
|
const double aqua = rates[Water];
|
|
const double liquid = rates[Oil];
|
|
const double vapour = rates[Gas];
|
|
|
|
// pick the density in the top layer
|
|
const double rho = perf_densities_[0];
|
|
|
|
double thp = 0.0;
|
|
if (well_type_ == INJECTOR) {
|
|
const int table_id = well_ecl_.vfp_table_number();
|
|
const double vfp_ref_depth = vfp_properties_->getInj()->getTable(table_id)->getDatumDepth();
|
|
const double dp = wellhelpers::computeHydrostaticCorrection(ref_depth_, vfp_ref_depth, rho, gravity_);
|
|
|
|
thp = vfp_properties_->getInj()->thp(table_id, aqua, liquid, vapour, bhp + dp);
|
|
}
|
|
else if (well_type_ == PRODUCER) {
|
|
const int table_id = well_ecl_.vfp_table_number();
|
|
const double alq = well_ecl_.alq_value();
|
|
const double vfp_ref_depth = vfp_properties_->getProd()->getTable(table_id)->getDatumDepth();
|
|
const double dp = wellhelpers::computeHydrostaticCorrection(ref_depth_, vfp_ref_depth, rho, gravity_);
|
|
|
|
thp = vfp_properties_->getProd()->thp(table_id, aqua, liquid, vapour, bhp + dp, alq);
|
|
}
|
|
else {
|
|
OPM_DEFLOG_THROW(std::logic_error, "Expected INJECTOR or PRODUCER well", deferred_logger);
|
|
}
|
|
|
|
return thp;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateWaterMobilityWithPolymer(const Simulator& ebos_simulator,
|
|
const int perf,
|
|
std::vector<EvalWell>& mob,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
// for the cases related to polymer molecular weight, we assume fully mixing
|
|
// as a result, the polymer and water share the same viscosity
|
|
if (this->has_polymermw) {
|
|
return;
|
|
}
|
|
const int cell_idx = well_cells_[perf];
|
|
const auto& int_quant = *(ebos_simulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/ 0));
|
|
const EvalWell polymer_concentration = extendEval(int_quant.polymerConcentration());
|
|
|
|
// TODO: not sure should based on the well type or injecting/producing peforations
|
|
// it can be different for crossflow
|
|
if (well_type_ == INJECTOR) {
|
|
// assume fully mixing within injecting wellbore
|
|
const auto& visc_mult_table = PolymerModule::plyviscViscosityMultiplierTable(int_quant.pvtRegionIndex());
|
|
const unsigned waterCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx);
|
|
mob[waterCompIdx] /= (extendEval(int_quant.waterViscosityCorrection()) * visc_mult_table.eval(polymer_concentration, /*extrapolate=*/true) );
|
|
}
|
|
|
|
if (PolymerModule::hasPlyshlog()) {
|
|
// we do not calculate the shear effects for injection wells when they do not
|
|
// inject polymer.
|
|
if (well_type_ == INJECTOR && wpolymer() == 0.) {
|
|
return;
|
|
}
|
|
// compute the well water velocity with out shear effects.
|
|
// TODO: do we need to turn on crossflow here?
|
|
const bool allow_cf = getAllowCrossFlow() || openCrossFlowAvoidSingularity(ebos_simulator);
|
|
const EvalWell& bhp = getBhp();
|
|
|
|
std::vector<EvalWell> cq_s(num_components_, {numWellEq_ + numEq, 0.});
|
|
double perf_dis_gas_rate = 0.;
|
|
double perf_vap_oil_rate = 0.;
|
|
double trans_mult = ebos_simulator.problem().template rockCompTransMultiplier<double>(int_quant, cell_idx);
|
|
const double Tw = well_index_[perf] * trans_mult;
|
|
computePerfRate(int_quant, mob, bhp, Tw, perf, allow_cf,
|
|
cq_s, perf_dis_gas_rate, perf_vap_oil_rate, deferred_logger);
|
|
// TODO: make area a member
|
|
const double area = 2 * M_PI * perf_rep_radius_[perf] * perf_length_[perf];
|
|
const auto& material_law_manager = ebos_simulator.problem().materialLawManager();
|
|
const auto& scaled_drainage_info =
|
|
material_law_manager->oilWaterScaledEpsInfoDrainage(cell_idx);
|
|
const double swcr = scaled_drainage_info.Swcr;
|
|
const EvalWell poro = extendEval(int_quant.porosity());
|
|
const EvalWell sw = extendEval(int_quant.fluidState().saturation(FluidSystem::waterPhaseIdx));
|
|
// guard against zero porosity and no water
|
|
const EvalWell denom = Opm::max( (area * poro * (sw - swcr)), 1e-12);
|
|
const unsigned waterCompIdx = Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx);
|
|
EvalWell water_velocity = cq_s[waterCompIdx] / denom * extendEval(int_quant.fluidState().invB(FluidSystem::waterPhaseIdx));
|
|
|
|
if (PolymerModule::hasShrate()) {
|
|
// the equation for the water velocity conversion for the wells and reservoir are from different version
|
|
// of implementation. It can be changed to be more consistent when possible.
|
|
water_velocity *= PolymerModule::shrate( int_quant.pvtRegionIndex() ) / bore_diameters_[perf];
|
|
}
|
|
const EvalWell shear_factor = PolymerModule::computeShearFactor(polymer_concentration,
|
|
int_quant.pvtRegionIndex(),
|
|
water_velocity);
|
|
// modify the mobility with the shear factor.
|
|
mob[waterCompIdx] /= shear_factor;
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::addWellContributions(SparseMatrixAdapter& jacobian) const
|
|
{
|
|
// We need to change matrx A as follows
|
|
// A -= C^T D^-1 B
|
|
// D is diagonal
|
|
// B and C have 1 row, nc colums and nonzero
|
|
// at (0,j) only if this well has a perforation at cell j.
|
|
|
|
typename SparseMatrixAdapter::MatrixBlock tmpMat;
|
|
Dune::DynamicMatrix<Scalar> tmp;
|
|
for ( auto colC = duneC_[0].begin(), endC = duneC_[0].end(); colC != endC; ++colC )
|
|
{
|
|
const auto row_index = colC.index();
|
|
|
|
for ( auto colB = duneB_[0].begin(), endB = duneB_[0].end(); colB != endB; ++colB )
|
|
{
|
|
Detail::multMatrix(invDuneD_[0][0], (*colB), tmp);
|
|
Detail::negativeMultMatrixTransposed((*colC), tmp, tmpMat);
|
|
jacobian.addToBlock( row_index, colB.index(), tmpMat );
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
double
|
|
StandardWell<TypeTag>::
|
|
relaxationFactorFraction(const double old_value,
|
|
const double dx)
|
|
{
|
|
assert(old_value >= 0. && old_value <= 1.0);
|
|
|
|
double relaxation_factor = 1.;
|
|
|
|
// updated values without relaxation factor
|
|
const double possible_updated_value = old_value - dx;
|
|
|
|
// 0.95 is an experimental value remains to be optimized
|
|
if (possible_updated_value < 0.0) {
|
|
relaxation_factor = std::abs(old_value / dx) * 0.95;
|
|
} else if (possible_updated_value > 1.0) {
|
|
relaxation_factor = std::abs((1. - old_value) / dx) * 0.95;
|
|
}
|
|
// if possible_updated_value is between 0. and 1.0, then relaxation_factor
|
|
// remains to be one
|
|
|
|
assert(relaxation_factor >= 0. && relaxation_factor <= 1.);
|
|
|
|
return relaxation_factor;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
double
|
|
StandardWell<TypeTag>::
|
|
relaxationFactorFractionsProducer(const std::vector<double>& primary_variables,
|
|
const BVectorWell& dwells)
|
|
{
|
|
// TODO: not considering solvent yet
|
|
// 0.95 is a experimental value, which remains to be optimized
|
|
double relaxation_factor = 1.0;
|
|
|
|
if (FluidSystem::numActivePhases() > 1) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
const double relaxation_factor_w = relaxationFactorFraction(primary_variables[WFrac], dwells[0][WFrac]);
|
|
relaxation_factor = std::min(relaxation_factor, relaxation_factor_w);
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
const double relaxation_factor_g = relaxationFactorFraction(primary_variables[GFrac], dwells[0][GFrac]);
|
|
relaxation_factor = std::min(relaxation_factor, relaxation_factor_g);
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)
|
|
&& FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
// We need to make sure the even with the relaxation_factor, the sum of F_w and F_g is below one, so
|
|
// there will not be negative oil fraction later
|
|
const double original_sum = primary_variables[WFrac] + primary_variables[GFrac];
|
|
const double relaxed_update = (dwells[0][WFrac] + dwells[0][GFrac]) * relaxation_factor;
|
|
const double possible_updated_sum = original_sum - relaxed_update;
|
|
|
|
if (possible_updated_sum > 1.0) {
|
|
assert(relaxed_update != 0.);
|
|
|
|
const double further_relaxation_factor = std::abs((1. - original_sum) / relaxed_update) * 0.95;
|
|
relaxation_factor *= further_relaxation_factor;
|
|
}
|
|
}
|
|
}
|
|
|
|
assert(relaxation_factor >= 0.0 && relaxation_factor <= 1.0);
|
|
|
|
return relaxation_factor;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
double
|
|
StandardWell<TypeTag>::
|
|
relaxationFactorRate(const std::vector<double>& primary_variables,
|
|
const BVectorWell& dwells)
|
|
{
|
|
double relaxation_factor = 1.0;
|
|
|
|
// For injector, we only check the total rates to avoid sign change of rates
|
|
const double original_total_rate = primary_variables[WQTotal];
|
|
const double newton_update = dwells[0][WQTotal];
|
|
const double possible_update_total_rate = primary_variables[WQTotal] - newton_update;
|
|
|
|
// 0.8 here is a experimental value, which remains to be optimized
|
|
// if the original rate is zero or possible_update_total_rate is zero, relaxation_factor will
|
|
// always be 1.0, more thoughts might be needed.
|
|
if (original_total_rate * possible_update_total_rate < 0.) { // sign changed
|
|
relaxation_factor = std::abs(original_total_rate / newton_update) * 0.8;
|
|
}
|
|
|
|
assert(relaxation_factor >= 0.0 && relaxation_factor <= 1.0);
|
|
|
|
return relaxation_factor;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
wellTestingPhysical(const Simulator& ebos_simulator, const std::vector<double>& B_avg,
|
|
const double /* simulation_time */, const int /* report_step */,
|
|
WellState& well_state, WellTestState& welltest_state,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
deferred_logger.info(" well " + name() + " is being tested for physical limits");
|
|
|
|
// some most difficult things are the explicit quantities, since there is no information
|
|
// in the WellState to do a decent initialization
|
|
|
|
// TODO: Let us assume that the simulator is updated
|
|
|
|
// Let us try to do a normal simualtion running, to keep checking the operability status
|
|
// If the well is not operable during any of the time. It means it does not pass the physical
|
|
// limit test.
|
|
|
|
// create a copy of the well_state to use. If the operability checking is sucessful, we use this one
|
|
// to replace the original one
|
|
WellState well_state_copy = well_state;
|
|
|
|
// TODO: well state for this well is kind of all zero status
|
|
// we should be able to provide a better initialization
|
|
calculateExplicitQuantities(ebos_simulator, well_state_copy, deferred_logger);
|
|
|
|
updateWellOperability(ebos_simulator, well_state_copy, deferred_logger);
|
|
|
|
if ( !this->isOperable() ) {
|
|
const std::string msg = " well " + name() + " is not operable during well testing for physical reason";
|
|
deferred_logger.debug(msg);
|
|
return;
|
|
}
|
|
|
|
updateWellStateWithTarget(ebos_simulator, well_state_copy, deferred_logger);
|
|
|
|
calculateExplicitQuantities(ebos_simulator, well_state_copy, deferred_logger);
|
|
updatePrimaryVariables(well_state_copy, deferred_logger);
|
|
initPrimaryVariablesEvaluation();
|
|
|
|
const bool converged = this->solveWellEqUntilConverged(ebos_simulator, B_avg, well_state_copy, deferred_logger);
|
|
|
|
if (!converged) {
|
|
const std::string msg = " well " + name() + " did not get converged during well testing for physical reason";
|
|
deferred_logger.debug(msg);
|
|
return;
|
|
}
|
|
|
|
if (this->isOperable() ) {
|
|
welltest_state.openWell(name(), WellTestConfig::PHYSICAL );
|
|
const std::string msg = " well " + name() + " is re-opened through well testing for physical reason";
|
|
deferred_logger.info(msg);
|
|
well_state = well_state_copy;
|
|
} else {
|
|
const std::string msg = " well " + name() + " is not operable during well testing for physical reason";
|
|
deferred_logger.debug(msg);
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
typename StandardWell<TypeTag>::EvalWell
|
|
StandardWell<TypeTag>::
|
|
pskinwater(const double throughput,
|
|
const EvalWell& water_velocity,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
if (!this->has_polymermw) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Polymermw is not activated, "
|
|
"while injecting skin pressure is requested for well " << name(), deferred_logger);
|
|
}
|
|
const int water_table_id = well_ecl_.getPolymerProperties().m_skprwattable;
|
|
if (water_table_id <= 0) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Unused SKPRWAT table id used for well " << name(), deferred_logger);
|
|
}
|
|
const auto& water_table_func = PolymerModule::getSkprwatTable(water_table_id);
|
|
const EvalWell throughput_eval(numWellEq_ + numEq, throughput);
|
|
// the skin pressure when injecting water, which also means the polymer concentration is zero
|
|
EvalWell pskin_water(numWellEq_ + numEq, 0.0);
|
|
pskin_water = water_table_func.eval(throughput_eval, water_velocity);
|
|
return pskin_water;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
typename StandardWell<TypeTag>::EvalWell
|
|
StandardWell<TypeTag>::
|
|
pskin(const double throughput,
|
|
const EvalWell& water_velocity,
|
|
const EvalWell& poly_inj_conc,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
if (!this->has_polymermw) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Polymermw is not activated, "
|
|
"while injecting skin pressure is requested for well " << name(), deferred_logger);
|
|
}
|
|
const double sign = water_velocity >= 0. ? 1.0 : -1.0;
|
|
const EvalWell water_velocity_abs = Opm::abs(water_velocity);
|
|
if (poly_inj_conc == 0.) {
|
|
return sign * pskinwater(throughput, water_velocity_abs, deferred_logger);
|
|
}
|
|
const int polymer_table_id = well_ecl_.getPolymerProperties().m_skprpolytable;
|
|
if (polymer_table_id <= 0) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Unavailable SKPRPOLY table id used for well " << name(), deferred_logger);
|
|
}
|
|
const auto& skprpolytable = PolymerModule::getSkprpolyTable(polymer_table_id);
|
|
const double reference_concentration = skprpolytable.refConcentration;
|
|
const EvalWell throughput_eval(numWellEq_ + numEq, throughput);
|
|
// the skin pressure when injecting water, which also means the polymer concentration is zero
|
|
EvalWell pskin_poly(numWellEq_ + numEq, 0.0);
|
|
pskin_poly = skprpolytable.table_func.eval(throughput_eval, water_velocity_abs);
|
|
if (poly_inj_conc == reference_concentration) {
|
|
return sign * pskin_poly;
|
|
}
|
|
// poly_inj_conc != reference concentration of the table, then some interpolation will be required
|
|
const EvalWell pskin_water = pskinwater(throughput, water_velocity_abs, deferred_logger);
|
|
const EvalWell pskin = pskin_water + (pskin_poly - pskin_water) / reference_concentration * poly_inj_conc;
|
|
return sign * pskin;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
typename StandardWell<TypeTag>::EvalWell
|
|
StandardWell<TypeTag>::
|
|
wpolymermw(const double throughput,
|
|
const EvalWell& water_velocity,
|
|
Opm::DeferredLogger& deferred_logger) const
|
|
{
|
|
if (!this->has_polymermw) {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Polymermw is not activated, "
|
|
"while injecting polymer molecular weight is requested for well " << name(), deferred_logger);
|
|
}
|
|
const int table_id = well_ecl_.getPolymerProperties().m_plymwinjtable;
|
|
const auto& table_func = PolymerModule::getPlymwinjTable(table_id);
|
|
const EvalWell throughput_eval(numWellEq_ + numEq, throughput);
|
|
EvalWell molecular_weight(numWellEq_ + numEq, 0.);
|
|
if (wpolymer() == 0.) { // not injecting polymer
|
|
return molecular_weight;
|
|
}
|
|
molecular_weight = table_func.eval(throughput_eval, Opm::abs(water_velocity));
|
|
return molecular_weight;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
updateWaterThroughput(const double dt, WellState &well_state) const
|
|
{
|
|
if (this->has_polymermw && well_type_ == INJECTOR) {
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
const double perf_water_vel = primary_variables_[Bhp + 1 + perf];
|
|
// we do not consider the formation damage due to water flowing from reservoir into wellbore
|
|
if (perf_water_vel > 0.) {
|
|
well_state.perfThroughput()[first_perf_ + perf] += perf_water_vel * dt;
|
|
}
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
handleInjectivityRateAndEquations(const IntensiveQuantities& int_quants,
|
|
const WellState& well_state,
|
|
const int perf,
|
|
std::vector<EvalWell>& cq_s,
|
|
Opm::DeferredLogger& deferred_logger)
|
|
{
|
|
const unsigned water_comp_idx = Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx);
|
|
const EvalWell& water_flux_s = cq_s[water_comp_idx];
|
|
const auto& fs = int_quants.fluidState();
|
|
const EvalWell b_w = extendEval(fs.invB(FluidSystem::waterPhaseIdx));
|
|
const EvalWell water_flux_r = water_flux_s / b_w;
|
|
const double area = M_PI * bore_diameters_[perf] * perf_length_[perf];
|
|
const EvalWell water_velocity = water_flux_r / area;
|
|
const int wat_vel_index = Bhp + 1 + perf;
|
|
|
|
// equation for the water velocity
|
|
const EvalWell eq_wat_vel = primary_variables_evaluation_[wat_vel_index] - water_velocity;
|
|
resWell_[0][wat_vel_index] = eq_wat_vel.value();
|
|
|
|
const double throughput = well_state.perfThroughput()[first_perf_ + perf];
|
|
const int pskin_index = Bhp + 1 + number_of_perforations_ + perf;
|
|
|
|
EvalWell poly_conc(numWellEq_ + numEq, 0.0);
|
|
poly_conc.setValue(wpolymer());
|
|
|
|
// equation for the skin pressure
|
|
const EvalWell eq_pskin = primary_variables_evaluation_[pskin_index]
|
|
- pskin(throughput, primary_variables_evaluation_[wat_vel_index], poly_conc, deferred_logger);
|
|
|
|
resWell_[0][pskin_index] = eq_pskin.value();
|
|
for (int pvIdx = 0; pvIdx < numWellEq_; ++pvIdx) {
|
|
invDuneD_[0][0][wat_vel_index][pvIdx] = eq_wat_vel.derivative(pvIdx+numEq);
|
|
invDuneD_[0][0][pskin_index][pvIdx] = eq_pskin.derivative(pvIdx+numEq);
|
|
}
|
|
|
|
// water rate is update to use the form from water velocity, since water velocity is
|
|
// a primary variable now
|
|
cq_s[water_comp_idx] = area * primary_variables_evaluation_[wat_vel_index] * b_w;
|
|
|
|
// the water velocity is impacted by the reservoir primary varaibles. It needs to enter matrix B
|
|
const int cell_idx = well_cells_[perf];
|
|
for (int pvIdx = 0; pvIdx < numEq; ++pvIdx) {
|
|
duneB_[0][cell_idx][wat_vel_index][pvIdx] = eq_wat_vel.derivative(pvIdx);
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
checkConvergenceControlEq(ConvergenceReport& report,
|
|
DeferredLogger& deferred_logger) const
|
|
{
|
|
double control_tolerance = 0.;
|
|
using CR = ConvergenceReport;
|
|
CR::WellFailure::Type ctrltype = CR::WellFailure::Type::Invalid;
|
|
switch(well_controls_get_current_type(well_controls_)) {
|
|
case THP:
|
|
ctrltype = CR::WellFailure::Type::ControlTHP;
|
|
control_tolerance = 1.e4; // 0.1 bar
|
|
break;
|
|
case BHP: // pressure type of control
|
|
ctrltype = CR::WellFailure::Type::ControlBHP;
|
|
control_tolerance = 1.e3; // 0.01 bar
|
|
break;
|
|
case RESERVOIR_RATE:
|
|
case SURFACE_RATE:
|
|
ctrltype = CR::WellFailure::Type::ControlRate;
|
|
control_tolerance = 1.e-4; // smaller tolerance for rate control
|
|
break;
|
|
default:
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Unknown well control control types for well " << name(), deferred_logger);
|
|
}
|
|
assert(ctrltype != CR::WellFailure::Type::Invalid);
|
|
|
|
const double well_control_residual = std::abs(resWell_[0][Bhp]);
|
|
const int dummy_component = -1;
|
|
const double max_residual_allowed = param_.max_residual_allowed_;
|
|
if (std::isnan(well_control_residual)) {
|
|
report.setWellFailed({ctrltype, CR::Severity::NotANumber, dummy_component, name()});
|
|
} else if (well_control_residual > max_residual_allowed * 10.) {
|
|
report.setWellFailed({ctrltype, CR::Severity::TooLarge, dummy_component, name()});
|
|
} else if ( well_control_residual > control_tolerance) {
|
|
report.setWellFailed({ctrltype, CR::Severity::Normal, dummy_component, name()});
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template<typename TypeTag>
|
|
void
|
|
StandardWell<TypeTag>::
|
|
checkConvergenceExtraEqs(const std::vector<double>& res,
|
|
ConvergenceReport& report) const
|
|
{
|
|
// if different types of extra equations are involved, this function needs to be refactored further
|
|
|
|
// checking the convergence of the extra equations related to polymer injectivity
|
|
if (this->has_polymermw && well_type_ == INJECTOR) {
|
|
// checking the convergence of the perforation rates
|
|
const double wat_vel_tol = 1.e-8;
|
|
const int dummy_component = -1;
|
|
const double maxResidualAllowed = param_.max_residual_allowed_;
|
|
using CR = ConvergenceReport;
|
|
const auto wat_vel_failure_type = CR::WellFailure::Type::MassBalance;
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
const double wat_vel_residual = res[Bhp + 1 + perf];
|
|
if (std::isnan(wat_vel_residual)) {
|
|
report.setWellFailed({wat_vel_failure_type, CR::Severity::NotANumber, dummy_component, name()});
|
|
} else if (wat_vel_residual > maxResidualAllowed * 10.) {
|
|
report.setWellFailed({wat_vel_failure_type, CR::Severity::TooLarge, dummy_component, name()});
|
|
} else if (wat_vel_residual > wat_vel_tol) {
|
|
report.setWellFailed({wat_vel_failure_type, CR::Severity::Normal, dummy_component, name()});
|
|
}
|
|
}
|
|
|
|
// checking the convergence of the skin pressure
|
|
const double pskin_tol = 1000.; // 1000 pascal
|
|
const auto pskin_failure_type = CR::WellFailure::Type::Pressure;
|
|
for (int perf = 0; perf < number_of_perforations_; ++perf) {
|
|
const double pskin_residual = res[Bhp + 1 + perf + number_of_perforations_];
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if (std::isnan(pskin_residual)) {
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report.setWellFailed({pskin_failure_type, CR::Severity::NotANumber, dummy_component, name()});
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} else if (pskin_residual > maxResidualAllowed * 10.) {
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report.setWellFailed({pskin_failure_type, CR::Severity::TooLarge, dummy_component, name()});
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} else if (pskin_residual > pskin_tol) {
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report.setWellFailed({pskin_failure_type, CR::Severity::Normal, dummy_component, name()});
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}
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}
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}
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}
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template<typename TypeTag>
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void
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StandardWell<TypeTag>::
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updateConnectionRatePolyMW(const EvalWell& cq_s_poly,
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const IntensiveQuantities& int_quants,
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const WellState& well_state,
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const int perf,
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|
DeferredLogger& deferred_logger)
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{
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// the source term related to transport of molecular weight
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EvalWell cq_s_polymw = cq_s_poly;
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if (well_type_ == INJECTOR) {
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|
const int wat_vel_index = Bhp + 1 + perf;
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const EvalWell water_velocity = primary_variables_evaluation_[wat_vel_index];
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if (water_velocity > 0.) { // injecting
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const double throughput = well_state.perfThroughput()[first_perf_ + perf];
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const EvalWell molecular_weight = wpolymermw(throughput, water_velocity, deferred_logger);
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cq_s_polymw *= molecular_weight;
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} else {
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// we do not consider the molecular weight from the polymer
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|
// going-back to the wellbore through injector
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|
cq_s_polymw *= 0.;
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}
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} else if (well_type_ == PRODUCER) {
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if (cq_s_polymw < 0.) {
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cq_s_polymw *= extendEval(int_quants.polymerMoleWeight() );
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} else {
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// we do not consider the molecular weight from the polymer
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|
// re-injecting back through producer
|
|
cq_s_polymw *= 0.;
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|
}
|
|
}
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|
connectionRates_[perf][this->contiPolymerMWEqIdx] = Base::restrictEval(cq_s_polymw);
|
|
}
|
|
}
|