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adding function updateIPR() to StandardWell
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@ -257,6 +257,13 @@ 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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// the vectors used to describe the inflow performance relationship (IPR)
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// Q = IPR_A - BHP * IPR_B
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// TODO: it minght need to go to WellInterface, let us implement it in StandardWell first
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// it is only updated and used for producers for now
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mutable std::vector<double> ipr_a_;
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mutable std::vector<double> ipr_b_;
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const EvalWell& getBhp() const;
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EvalWell getQs(const int comp_idx) const;
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@ -354,6 +361,9 @@ namespace Opm
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// handle the non reasonable fractions due to numerical overshoot
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void processFractions() const;
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// updating the inflow based on the current reservoir condition
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void updateIPR(const Simulator& ebos_simulator) const;
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// relaxation factor considering only one fraction value
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static double relaxationFactorFraction(const double old_value,
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const double dx);
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@ -36,6 +36,8 @@ namespace Opm
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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_(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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@ -1229,6 +1231,100 @@ namespace Opm
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template<typename TypeTag>
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void
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StandardWell<TypeTag>::
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updateIPR(const Simulator& ebos_simulator) const
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{
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// TODO: not handling solvent related here for now
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// TODO: it only handles the producers for now
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// the formular for the injectors are not formulated yet
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if (well_type_ == INJECTOR) {
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return;
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}
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// initialize all the values to be zero to begin with
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std::fill(ipr_a_.begin(), ipr_a_.end(), 0.);
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std::fill(ipr_b_.begin(), ipr_b_.end(), 0.);
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for (int perf = 0; perf < number_of_perforations_; ++perf) {
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std::vector<EvalWell> mob(num_components_, 0.0);
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// TODO: mabye we should store the mobility somewhere, so that we only need to calculate it one per iteration
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getMobility(ebos_simulator, perf, mob);
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const int cell_idx = well_cells_[perf];
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const auto& int_quantities = *(ebos_simulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/ 0));
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const auto& fs = int_quantities.fluidState();
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// the pressure of the reservoir grid block the well connection is in
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const double p_r = fs.pressure(FluidSystem::oilPhaseIdx).value();
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// calculating the b for the connection
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std::vector<double> b_perf(num_components_);
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for (int phase = 0; phase < FluidSystem::numPhases; ++phase) {
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if (!FluidSystem::phaseIsActive(phase)) {
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continue;
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}
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const unsigned comp_idx = Indices::canonicalToActiveComponentIndex(FluidSystem::solventComponentIndex(phase));
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b_perf[comp_idx] = fs.invB(phase).value();
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}
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// the pressure difference between the connection and BHP
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const double h_perf = perf_pressure_diffs_[perf];
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const double pressure_diff = p_r - h_perf;
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// Let us add a check, since the pressure is calculated based on zero value BHP
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// it should not be negative anyway. If it is negative, we might need to re-formulate
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// to taking into consideration the crossflow here.
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if (pressure_diff <= 0.) {
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OpmLog::warning("NON_POSITIVE_DRAWDOWN_IPR", "non-positive drawdown found when updateIPR for well " + name());
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}
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// the well index associated with the connection
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const double tw_perf = well_index_[perf];
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// TODO: there might be some indices related problems here
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// phases vs components
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// ipr values for the perforation
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std::vector<double> ipr_a_perf(ipr_a_.size());
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std::vector<double> ipr_b_perf(ipr_b_.size());
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for (int p = 0; p < number_of_phases_; ++p) {
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const double tw_mob = tw_perf * mob[p].value() * b_perf[p];
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ipr_a_perf[p] += tw_mob * pressure_diff;
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ipr_b_perf[p] += tw_mob;
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}
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// we need to handle the rs and rv when both oil and gas are present
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if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) && FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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const unsigned oil_comp_idx = Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx);
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const unsigned gas_comp_idx = Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx);
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const double rs = (fs.Rs()).value();
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const double rv = (fs.Rv()).value();
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const double dis_gas_a = rs * ipr_a_perf[oil_comp_idx];
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const double vap_oil_a = rv * ipr_a_perf[gas_comp_idx];
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ipr_a_perf[gas_comp_idx] += dis_gas_a;
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ipr_a_perf[oil_comp_idx] += vap_oil_a;
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const double dis_gas_b = rs * ipr_b_perf[oil_comp_idx];
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const double vap_oil_b = rv * ipr_b_perf[gas_comp_idx];
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ipr_b_perf[gas_comp_idx] += dis_gas_b;
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ipr_b_perf[oil_comp_idx] += vap_oil_b;
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}
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for (int p = 0; p < number_of_phases_; ++p) {
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ipr_a_[p] += ipr_a_perf[p];
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ipr_b_[p] += ipr_b_perf[p];
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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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