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Move Rateconverter and pvtIdx to the wellInterface
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054361d537
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@ -221,13 +221,14 @@ namespace Opm {
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const Well* well_ecl = wells_ecl_[index_well];
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// Use the pvtRegionIdx from the top cell
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const int well_cell_top = wells()->well_cells[wells()->well_connpos[w]];
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const int pvtreg = pvt_region_idx_[well_cell_top];
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if ( !well_ecl->isMultiSegment(time_step) || !param_.use_multisegment_well_) {
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well_container.emplace_back(new StandardWell<TypeTag>(well_ecl, time_step, wells(), param_, *rateConverter_, pvtreg ) );
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} else {
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well_container.emplace_back(new MultisegmentWell<TypeTag>(well_ecl, time_step, wells(), param_) );
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well_container.emplace_back(new MultisegmentWell<TypeTag>(well_ecl, time_step, wells(), param_, *rateConverter_, pvtreg) );
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}
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}
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}
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@ -41,6 +41,8 @@ namespace Opm
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using typename Base::ModelParameters;
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using typename Base::MaterialLaw;
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using typename Base::BlackoilIndices;
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using typename Base::RateConverterType;
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/// the number of reservior equations
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using Base::numEq;
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@ -97,7 +99,10 @@ namespace Opm
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// TODO: for now, we only use one type to save some implementation efforts, while improve later.
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typedef DenseAd::Evaluation<double, /*size=*/numEq + numWellEq> EvalWell;
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MultisegmentWell(const Well* well, const int time_step, const Wells* wells, const ModelParameters& param);
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MultisegmentWell(const Well* 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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virtual void init(const PhaseUsage* phase_usage_arg,
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const std::vector<bool>* active_arg,
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@ -188,6 +193,7 @@ namespace Opm
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using Base::flowPhaseToEbosPhaseIdx;
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using Base::flowPhaseToEbosCompIdx;
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using Base::getAllowCrossFlow;
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using Base::scalingFactor;
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// TODO: trying to use the information from the Well opm-parser as much
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// as possible, it will possibly be re-implemented later for efficiency reason.
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@ -329,8 +335,6 @@ namespace Opm
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void updateWellStateFromPrimaryVariables(WellState& well_state) const;
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double scalingFactor(const int comp_idx) const;
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bool frictionalPressureLossConsidered() const;
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bool accelerationalPressureLossConsidered() const;
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@ -27,8 +27,11 @@ namespace Opm
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template <typename TypeTag>
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MultisegmentWell<TypeTag>::
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MultisegmentWell(const Well* well, const int time_step, const Wells* wells, const ModelParameters& param)
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: Base(well, time_step, wells, param)
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MultisegmentWell(const Well* 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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: Base(well, time_step, wells, param, rate_converter, pvtRegionIdx)
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, segment_perforations_(numberOfSegments())
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, segment_inlets_(numberOfSegments())
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, cell_perforation_depth_diffs_(number_of_perforations_, 0.0)
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@ -1666,40 +1669,6 @@ namespace Opm
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template <typename TypeTag>
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double
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MultisegmentWell<TypeTag>::
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scalingFactor(const int comp_idx) const
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{
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const double* distr = well_controls_get_current_distr(well_controls_);
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if (well_controls_get_current_type(well_controls_) == RESERVOIR_RATE) {
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// if (has_solvent && phaseIdx == contiSolventEqIdx )
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// OPM_THROW(std::runtime_error, "RESERVOIR_RATE control in combination with solvent is not implemented");
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return distr[comp_idx];
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}
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const PhaseUsage& pu = phaseUsage();
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if (active()[Water] && pu.phase_pos[Water] == comp_idx)
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return 1.0;
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if (active()[Oil] && pu.phase_pos[Oil] == comp_idx)
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return 1.0;
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if (active()[Gas] && pu.phase_pos[Gas] == comp_idx)
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return 0.01;
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// if (has_solvent && phaseIdx == contiSolventEqIdx )
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// return 0.01;
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// we should not come this far
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assert(false);
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return 1.0;
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}
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template <typename TypeTag>
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bool
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MultisegmentWell<TypeTag>::
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@ -48,6 +48,7 @@ namespace Opm
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using typename Base::ModelParameters;
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using typename Base::BlackoilIndices;
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using typename Base::PolymerModule;
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using typename Base::RateConverterType;
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using Base::numEq;
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@ -105,10 +106,6 @@ namespace Opm
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typedef DenseAd::Evaluation<double, /*size=*/numEq + numWellEq> EvalWell;
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// For the conversion between the surface volume rate and resrevoir voidage rate
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using RateConverterType = RateConverter::
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SurfaceToReservoirVoidage<FluidSystem, std::vector<int> >;
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// TODO: should these go to WellInterface?
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static const int contiSolventEqIdx = BlackoilIndices::contiSolventEqIdx;
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static const int contiPolymerEqIdx = BlackoilIndices::contiPolymerEqIdx;
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@ -177,6 +174,7 @@ namespace Opm
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using Base::wpolymer;
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using Base::wellHasTHPConstraints;
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using Base::mostStrictBhpFromBhpLimits;
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using Base::scalingFactor;
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// protected member variables from the Base class
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using Base::vfp_properties_;
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@ -228,9 +226,6 @@ namespace Opm
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// the saturations in the well bore under surface conditions at the beginning of the time step
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std::vector<double> F0_;
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const RateConverterType& rateConverter_;
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int pvtRegionIdx_;
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// TODO: this function should be moved to the base class.
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// while it faces chanllenges for MSWell later, since the calculation of bhp
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// based on THP is never implemented for MSWell yet.
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@ -313,7 +308,6 @@ namespace Opm
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const int perf,
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std::vector<EvalWell>& mob) const;
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double scalingFactor(const int comp_idx) const;
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};
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}
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@ -28,14 +28,12 @@ namespace Opm
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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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: Base(well, time_step, wells, param)
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: Base(well, time_step, wells, param, rate_converter, pvtRegionIdx)
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, perf_densities_(number_of_perforations_)
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, perf_pressure_diffs_(number_of_perforations_)
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, primary_variables_(numWellEq, 0.0)
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, primary_variables_evaluation_(numWellEq) // the number of the primary variables
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, F0_(numWellEq)
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, rateConverter_(rate_converter)
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, pvtRegionIdx_(pvtRegionIdx)
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{
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duneB_.setBuildMode( OffDiagMatWell::row_wise );
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duneC_.setBuildMode( OffDiagMatWell::row_wise );
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@ -1984,37 +1982,7 @@ namespace Opm
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return thp;
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}
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template<typename TypeTag>
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double
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StandardWell<TypeTag>::scalingFactor(const int phaseIdx) const
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{
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const WellControls* wc = well_controls_;
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const double* distr = well_controls_get_current_distr(wc);
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if (well_controls_get_current_type(wc) == RESERVOIR_RATE) {
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if (has_solvent && phaseIdx == contiSolventEqIdx ) {
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typedef Ewoms::BlackOilSolventModule<TypeTag> SolventModule;
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double coeff = 0;
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rateConverter_.template calcCoeffSolvent<SolventModule>(0, pvtRegionIdx_, coeff);
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return coeff;
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}
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// TODO: use the rateConverter here as well.
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return distr[phaseIdx];
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}
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const auto& pu = phaseUsage();
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if (active()[Water] && pu.phase_pos[Water] == phaseIdx)
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return 1.0;
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if (active()[Oil] && pu.phase_pos[Oil] == phaseIdx)
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return 1.0;
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if (active()[Gas] && pu.phase_pos[Gas] == phaseIdx)
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return 0.01;
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if (has_solvent && phaseIdx == contiSolventEqIdx )
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return 0.01;
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// we should not come this far
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assert(false);
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return 1.0;
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}
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}
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@ -1,6 +1,7 @@
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/*
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Copyright 2017 SINTEF Digital, Mathematics and Cybernetics.
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Copyright 2017 Statoil ASA.
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Copyright 2017 IRIS
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This file is part of the Open Porous Media project (OPM).
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@ -37,6 +38,7 @@
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#include <opm/autodiff/WellHelpers.hpp>
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#include <opm/autodiff/WellStateFullyImplicitBlackoil.hpp>
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#include <opm/autodiff/BlackoilModelParameters.hpp>
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#include <opm/autodiff/RateConverter.hpp>
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#include <opm/simulators/WellSwitchingLogger.hpp>
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@ -89,9 +91,18 @@ namespace Opm
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static const bool has_solvent = GET_PROP_VALUE(TypeTag, EnableSolvent);
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static const bool has_polymer = GET_PROP_VALUE(TypeTag, EnablePolymer);
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static const int contiSolventEqIdx = BlackoilIndices::contiSolventEqIdx;
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// For the conversion between the surface volume rate and resrevoir voidage rate
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using RateConverterType = RateConverter::
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SurfaceToReservoirVoidage<FluidSystem, std::vector<int> >;
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/// Constructor
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WellInterface(const Well* well, const int time_step, const Wells* wells, const ModelParameters& param);
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WellInterface(const Well* 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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/// Virutal destructor
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virtual ~WellInterface() {}
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@ -264,6 +275,13 @@ namespace Opm
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double gravity_;
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// For the conversion between the surface volume rate and resrevoir voidage rate
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const RateConverterType& rateConverter_;
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// The pvt region of the well. We assume
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// We assume a well to not penetrate more than one pvt region.
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int pvtRegionIdx_;
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const std::vector<bool>& active() const;
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const PhaseUsage& phaseUsage() const;
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@ -304,6 +322,9 @@ namespace Opm
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RatioCheckTuple checkRatioEconLimits(const WellEconProductionLimits& econ_production_limits,
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const WellState& well_state) const;
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double scalingFactor(const int comp_idx) const;
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};
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}
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@ -25,10 +25,15 @@ namespace Opm
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template<typename TypeTag>
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WellInterface<TypeTag>::
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WellInterface(const Well* well, const int time_step, const Wells* wells, const ModelParameters& param)
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WellInterface(const Well* 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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: well_ecl_(well)
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, current_step_(time_step)
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, param_(param)
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, rateConverter_(rate_converter)
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, pvtRegionIdx_(pvtRegionIdx)
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{
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if (!well) {
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OPM_THROW(std::invalid_argument, "Null pointer of Well is used to construct WellInterface");
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@ -850,4 +855,36 @@ namespace Opm
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}
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}
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template<typename TypeTag>
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double
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WellInterface<TypeTag>::scalingFactor(const int phaseIdx) const
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{
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const WellControls* wc = well_controls_;
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const double* distr = well_controls_get_current_distr(wc);
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if (well_controls_get_current_type(wc) == RESERVOIR_RATE) {
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if (has_solvent && phaseIdx == contiSolventEqIdx ) {
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typedef Ewoms::BlackOilSolventModule<TypeTag> SolventModule;
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double coeff = 0;
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rateConverter_.template calcCoeffSolvent<SolventModule>(0, pvtRegionIdx_, coeff);
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return coeff;
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}
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// TODO: use the rateConverter here as well.
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return distr[phaseIdx];
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}
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const auto& pu = phaseUsage();
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if (active()[Water] && pu.phase_pos[Water] == phaseIdx)
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return 1.0;
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if (active()[Oil] && pu.phase_pos[Oil] == phaseIdx)
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return 1.0;
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if (active()[Gas] && pu.phase_pos[Gas] == phaseIdx)
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return 0.01;
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if (has_solvent && phaseIdx == contiSolventEqIdx )
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return 0.01;
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// we should not come this far
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assert(false);
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return 1.0;
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}
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}
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