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Feed solvent wellrates to data::wells for summary output
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@ -625,6 +625,21 @@ namespace Opm {
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wellModel().updateWellState(dwells, dpMaxRel(), well_state);
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for( auto w = 0; w < wells().number_of_wells; ++w ) {
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if (wells().type[w] == INJECTOR) {
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continue;
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}
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for (int perf = wells().well_connpos[w]; perf < wells().well_connpos[w+1]; ++perf ) {
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int wc = wells().well_cells[perf];
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if ( (ss[wc] + sg[wc]) > 0) {
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well_state.solventFraction()[perf] = ss[wc] / (ss[wc] + sg[wc]);
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}
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}
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}
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// Update phase conditions used for property calculations.
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updatePhaseCondFromPrimalVariable(reservoir_state);
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}
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@ -33,6 +33,37 @@ namespace Opm
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/// One solvent fraction per well connection
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std::vector<double>& solventFraction() { return solvent_fraction_; }
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const std::vector<double>& solventFraction() const { return solvent_fraction_; }
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data::Wells report(const PhaseUsage &pu) const override {
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data::Wells res = WellStateFullyImplicitBlackoil::report(pu);
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const int nw = WellState::numWells();
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// If there are now wells numPhases throws a floating point
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// exception.
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if (nw == 0) {
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return res;
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}
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const int np = BaseType::numPhases();
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assert( np == 3 ); // the solvent model assumes 3 phases in the base model
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// completions aren't supported yet
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for( auto w = 0; w < nw; ++w ) {
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using rt = data::Rates::opt;
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double solvent_well_rate = 0.0;
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for (int perf = wells_->well_connpos[w]; perf < wells_->well_connpos[w+1]; ++perf ) {
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auto solvent_rate_this = BaseType::perfPhaseRates()[np*perf + pu.phase_pos[BlackoilPhases::Vapour]] * solventFraction()[perf];
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solvent_well_rate += solvent_rate_this;
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}
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res.at( wells_->name[ w ]).rates.set( rt::solvent, solvent_well_rate );
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}
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return res;
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}
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private:
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std::vector<double> solvent_fraction_;
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};
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