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564 lines
25 KiB
C++
564 lines
25 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 2018 IRIS
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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 <config.h>
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#include <opm/simulators/wells/WellInterfaceEval.hpp>
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#include <opm/material/densead/Evaluation.hpp>
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#include <opm/material/fluidsystems/BlackOilFluidSystem.hpp>
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#include <opm/parser/eclipse/EclipseState/Schedule/Schedule.hpp>
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#include <opm/simulators/utils/DeferredLoggingErrorHelpers.hpp>
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#include <opm/simulators/wells/GroupState.hpp>
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#include <opm/simulators/wells/RateConverter.hpp>
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#include <opm/simulators/wells/TargetCalculator.hpp>
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#include <opm/simulators/wells/VFPProperties.hpp>
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#include <opm/simulators/wells/WellGroupHelpers.hpp>
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#include <opm/simulators/wells/WellHelpers.hpp>
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#include <opm/simulators/wells/WellInterfaceFluidSystem.hpp>
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#include <opm/simulators/wells/WellState.hpp>
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#include <cassert>
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#include <cmath>
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#include <stdexcept>
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namespace Opm
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{
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template<class FluidSystem>
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WellInterfaceEval<FluidSystem>::
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WellInterfaceEval(const WellInterfaceFluidSystem<FluidSystem>& baseif)
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: baseif_(baseif)
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{}
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template<class FluidSystem>
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template<class EvalWell>
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void
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WellInterfaceEval<FluidSystem>::
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getGroupInjectionControl(const Group& group,
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const WellState& well_state,
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const GroupState& group_state,
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const Schedule& schedule,
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const SummaryState& summaryState,
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const InjectorType& injectorType,
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const EvalWell& bhp,
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const EvalWell& injection_rate,
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EvalWell& control_eq,
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double efficiencyFactor,
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DeferredLogger& deferred_logger) const
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{
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// Setting some defaults to silence warnings below.
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// Will be overwritten in the switch statement.
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Phase injectionPhase = Phase::WATER;
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switch (injectorType) {
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case InjectorType::WATER:
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{
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injectionPhase = Phase::WATER;
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break;
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}
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case InjectorType::OIL:
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{
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injectionPhase = Phase::OIL;
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break;
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}
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case InjectorType::GAS:
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{
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injectionPhase = Phase::GAS;
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break;
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}
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default:
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// Should not be here.
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assert(false);
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}
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auto currentGroupControl = group_state.injection_control(group.name(), injectionPhase);
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if (currentGroupControl == Group::InjectionCMode::FLD ||
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currentGroupControl == Group::InjectionCMode::NONE) {
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if (!group.injectionGroupControlAvailable(injectionPhase)) {
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// We cannot go any further up the hierarchy. This could
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// be the FIELD group, or any group for which this has
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// been set in GCONINJE or GCONPROD. If we are here
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// anyway, it is likely that the deck set inconsistent
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// requirements, such as GRUP control mode on a well with
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// no appropriate controls defined on any of its
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// containing groups. We will therefore use the wells' bhp
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// limit equation as a fallback.
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const auto& controls = baseif_.wellEcl().injectionControls(summaryState);
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control_eq = bhp - controls.bhp_limit;
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return;
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} else {
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// Inject share of parents control
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const auto& parent = schedule.getGroup( group.parent(), baseif_.currentStep());
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efficiencyFactor *= group.getGroupEfficiencyFactor();
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getGroupInjectionControl(parent, well_state, group_state, schedule, summaryState, injectorType, bhp, injection_rate, control_eq, efficiencyFactor, deferred_logger);
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return;
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}
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}
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const auto& well = baseif_.wellEcl();
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const auto pu = baseif_.phaseUsage();
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if (!group.isInjectionGroup()) {
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// use bhp as control eq and let the updateControl code find a valid control
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const auto& controls = well.injectionControls(summaryState);
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control_eq = bhp - controls.bhp_limit;
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return;
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}
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// If we are here, we are at the topmost group to be visited in the recursion.
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// This is the group containing the control we will check against.
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// Make conversion factors for RESV <-> surface rates.
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std::vector<double> resv_coeff(pu.num_phases, 1.0);
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baseif_.rateConverter().calcInjCoeff(0, baseif_.pvtRegionIdx(), resv_coeff); // FIPNUM region 0 here, should use FIPNUM from WELSPECS.
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double sales_target = 0;
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if (schedule[baseif_.currentStep()].gconsale().has(group.name())) {
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const auto& gconsale = schedule[baseif_.currentStep()].gconsale().get(group.name(), summaryState);
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sales_target = gconsale.sales_target;
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}
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WellGroupHelpers::InjectionTargetCalculator tcalc(currentGroupControl, pu, resv_coeff, group.name(), sales_target, group_state, injectionPhase, group.has_gpmaint_control(injectionPhase, currentGroupControl), deferred_logger);
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WellGroupHelpers::FractionCalculator fcalc(schedule, well_state, group_state, baseif_.currentStep(), baseif_.guideRate(), tcalc.guideTargetMode(), pu, false, injectionPhase);
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auto localFraction = [&](const std::string& child) {
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return fcalc.localFraction(child, child);
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};
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auto localReduction = [&](const std::string& group_name) {
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const std::vector<double>& groupTargetReductions = group_state.injection_reduction_rates(group_name);
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return tcalc.calcModeRateFromRates(groupTargetReductions);
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};
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const double orig_target = tcalc.groupTarget(group.injectionControls(injectionPhase, summaryState), deferred_logger);
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const auto chain = WellGroupHelpers::groupChainTopBot(baseif_.name(), group.name(), schedule, baseif_.currentStep());
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// Because 'name' is the last of the elements, and not an ancestor, we subtract one below.
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const size_t num_ancestors = chain.size() - 1;
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double target = orig_target;
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for (size_t ii = 0; ii < num_ancestors; ++ii) {
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if ((ii == 0) || baseif_.guideRate()->has(chain[ii], injectionPhase)) {
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// Apply local reductions only at the control level
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// (top) and for levels where we have a specified
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// group guide rate.
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target -= localReduction(chain[ii]);
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}
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target *= localFraction(chain[ii+1]);
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}
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// Avoid negative target rates coming from too large local reductions.
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const double target_rate = std::max(0.0, target / efficiencyFactor);
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const auto current_rate = injection_rate;
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control_eq = current_rate - target_rate;
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}
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template<class FluidSystem>
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template<class EvalWell>
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void
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WellInterfaceEval<FluidSystem>::
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getGroupProductionControl(const Group& group,
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const WellState& well_state,
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const GroupState& group_state,
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const Schedule& schedule,
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const SummaryState& summaryState,
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const EvalWell& bhp,
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const std::vector<EvalWell>& rates,
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EvalWell& control_eq,
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double efficiencyFactor) const
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{
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const Group::ProductionCMode& currentGroupControl = group_state.production_control(group.name());
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if (currentGroupControl == Group::ProductionCMode::FLD ||
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currentGroupControl == Group::ProductionCMode::NONE) {
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if (!group.productionGroupControlAvailable()) {
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// We cannot go any further up the hierarchy. This could
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// be the FIELD group, or any group for which this has
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// been set in GCONINJE or GCONPROD. If we are here
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// anyway, it is likely that the deck set inconsistent
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// requirements, such as GRUP control mode on a well with
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// no appropriate controls defined on any of its
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// containing groups. We will therefore use the wells' bhp
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// limit equation as a fallback.
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const auto& controls = baseif_.wellEcl().productionControls(summaryState);
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control_eq = bhp - controls.bhp_limit;
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return;
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} else {
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// Produce share of parents control
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const auto& parent = schedule.getGroup(group.parent(), baseif_.currentStep());
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efficiencyFactor *= group.getGroupEfficiencyFactor();
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getGroupProductionControl(parent, well_state, group_state, schedule, summaryState, bhp, rates, control_eq, efficiencyFactor);
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return;
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}
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}
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const auto& well = baseif_.wellEcl();
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const auto pu = baseif_.phaseUsage();
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if (!group.isProductionGroup()) {
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// use bhp as control eq and let the updateControl code find a valid control
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const auto& controls = well.productionControls(summaryState);
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control_eq = bhp - controls.bhp_limit;
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return;
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}
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// If we are here, we are at the topmost group to be visited in the recursion.
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// This is the group containing the control we will check against.
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// Make conversion factors for RESV <-> surface rates.
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std::vector<double> resv_coeff(baseif_.phaseUsage().num_phases, 1.0);
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baseif_.rateConverter().calcCoeff(0, baseif_.pvtRegionIdx(), resv_coeff); // FIPNUM region 0 here, should use FIPNUM from WELSPECS.
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// gconsale may adjust the grat target.
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// the adjusted rates is send to the targetCalculator
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double gratTargetFromSales = 0.0;
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if (group_state.has_grat_sales_target(group.name()))
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gratTargetFromSales = group_state.grat_sales_target(group.name());
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WellGroupHelpers::TargetCalculator tcalc(currentGroupControl, pu, resv_coeff, gratTargetFromSales, group.name(), group_state, group.has_gpmaint_control(currentGroupControl));
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WellGroupHelpers::FractionCalculator fcalc(schedule, well_state, group_state, baseif_.currentStep(), baseif_.guideRate(), tcalc.guideTargetMode(), pu, true, Phase::OIL);
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auto localFraction = [&](const std::string& child) {
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return fcalc.localFraction(child, child);
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};
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auto localReduction = [&](const std::string& group_name) {
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const std::vector<double>& groupTargetReductions = group_state.production_reduction_rates(group_name);
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return tcalc.calcModeRateFromRates(groupTargetReductions);
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};
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const double orig_target = tcalc.groupTarget(group.productionControls(summaryState));
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const auto chain = WellGroupHelpers::groupChainTopBot(baseif_.name(), group.name(), schedule, baseif_.currentStep());
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// Because 'name' is the last of the elements, and not an ancestor, we subtract one below.
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const size_t num_ancestors = chain.size() - 1;
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double target = orig_target;
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for (size_t ii = 0; ii < num_ancestors; ++ii) {
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if ((ii == 0) || baseif_.guideRate()->has(chain[ii])) {
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// Apply local reductions only at the control level
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// (top) and for levels where we have a specified
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// group guide rate.
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target -= localReduction(chain[ii]);
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}
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target *= localFraction(chain[ii+1]);
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}
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// Avoid negative target rates coming from too large local reductions.
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const double target_rate = std::max(0.0, target / efficiencyFactor);
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const auto current_rate = -tcalc.calcModeRateFromRates(rates); // Switch sign since 'rates' are negative for producers.
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control_eq = current_rate - target_rate;
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}
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template<class FluidSystem>
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template<class EvalWell>
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void
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WellInterfaceEval<FluidSystem>::
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assembleControlEqProd_(const WellState& well_state,
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const GroupState& group_state,
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const Schedule& schedule,
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const SummaryState& summaryState,
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const Well::ProductionControls& controls,
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const EvalWell& bhp,
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const std::vector<EvalWell>& rates, // Always 3 canonical rates.
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const std::function<EvalWell()>& bhp_from_thp,
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EvalWell& control_eq,
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DeferredLogger& deferred_logger) const
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{
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const auto current = well_state.well(baseif_.indexOfWell()).production_cmode;
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const auto& pu = baseif_.phaseUsage();
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const double efficiencyFactor = baseif_.wellEcl().getEfficiencyFactor();
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switch (current) {
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case Well::ProducerCMode::ORAT: {
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assert(FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx));
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const EvalWell rate = -rates[BlackoilPhases::Liquid];
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control_eq = rate - controls.oil_rate;
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break;
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}
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case Well::ProducerCMode::WRAT: {
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assert(FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx));
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const EvalWell rate = -rates[BlackoilPhases::Aqua];
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control_eq = rate - controls.water_rate;
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break;
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}
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case Well::ProducerCMode::GRAT: {
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assert(FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx));
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const EvalWell rate = -rates[BlackoilPhases::Vapour];
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control_eq = rate - controls.gas_rate;
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break;
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}
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case Well::ProducerCMode::LRAT: {
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assert(FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx));
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assert(FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx));
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EvalWell rate = -rates[BlackoilPhases::Aqua] - rates[BlackoilPhases::Liquid];
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control_eq = rate - controls.liquid_rate;
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break;
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}
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case Well::ProducerCMode::CRAT: {
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OPM_DEFLOG_THROW(std::runtime_error, "CRAT control not supported " << baseif_.name(), deferred_logger);
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}
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case Well::ProducerCMode::RESV: {
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auto total_rate = rates[0]; // To get the correct type only.
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total_rate = 0.0;
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std::vector<double> convert_coeff(baseif_.numPhases(), 1.0);
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baseif_.rateConverter().calcCoeff(/*fipreg*/ 0, baseif_.pvtRegionIdx(), convert_coeff);
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for (int phase = 0; phase < 3; ++phase) {
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if (pu.phase_used[phase]) {
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const int pos = pu.phase_pos[phase];
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total_rate -= rates[phase] * convert_coeff[pos]; // Note different indices.
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}
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}
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if (controls.prediction_mode) {
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control_eq = total_rate - controls.resv_rate;
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} else {
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std::vector<double> hrates(baseif_.numPhases(), 0.);
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if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
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hrates[pu.phase_pos[Water]] = controls.water_rate;
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}
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if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
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hrates[pu.phase_pos[Oil]] = controls.oil_rate;
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}
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if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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hrates[pu.phase_pos[Gas]] = controls.gas_rate;
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}
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std::vector<double> hrates_resv(baseif_.numPhases(), 0.);
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baseif_.rateConverter().calcReservoirVoidageRates(/*fipreg*/ 0, baseif_.pvtRegionIdx(), hrates, hrates_resv);
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double target = std::accumulate(hrates_resv.begin(), hrates_resv.end(), 0.0);
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control_eq = total_rate - target;
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}
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break;
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}
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case Well::ProducerCMode::BHP: {
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control_eq = bhp - controls.bhp_limit;
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break;
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}
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case Well::ProducerCMode::THP: {
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control_eq = bhp - bhp_from_thp();
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break;
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}
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case Well::ProducerCMode::GRUP: {
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assert(baseif_.wellEcl().isAvailableForGroupControl());
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const auto& group = schedule.getGroup(baseif_.wellEcl().groupName(), baseif_.currentStep());
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// Annoying thing: the rates passed to this function are
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// always of size 3 and in canonical (for PhaseUsage)
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// order. This is what is needed for VFP calculations if
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// they are required (THP controlled well). But for the
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// group production control things we must pass only the
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// active phases' rates.
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std::vector<EvalWell> active_rates(pu.num_phases);
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for (int canonical_phase = 0; canonical_phase < 3; ++canonical_phase) {
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if (pu.phase_used[canonical_phase]) {
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active_rates[pu.phase_pos[canonical_phase]] = rates[canonical_phase];
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}
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}
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getGroupProductionControl(group, well_state, group_state, schedule, summaryState, bhp, active_rates, control_eq, efficiencyFactor);
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break;
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}
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case Well::ProducerCMode::CMODE_UNDEFINED: {
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OPM_DEFLOG_THROW(std::runtime_error, "Well control must be specified for well " + baseif_.name(), deferred_logger);
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}
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case Well::ProducerCMode::NONE: {
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OPM_DEFLOG_THROW(std::runtime_error, "Well control must be specified for well " + baseif_.name(), deferred_logger);
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}
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}
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}
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template<class FluidSystem>
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template<class EvalWell>
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void
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WellInterfaceEval<FluidSystem>::
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assembleControlEqInj_(const WellState& well_state,
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const GroupState& group_state,
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const Schedule& schedule,
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const SummaryState& summaryState,
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const Well::InjectionControls& controls,
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const EvalWell& bhp,
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const EvalWell& injection_rate,
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const std::function<EvalWell()>& bhp_from_thp,
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EvalWell& control_eq,
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DeferredLogger& deferred_logger) const
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{
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auto current = well_state.well(baseif_.indexOfWell()).injection_cmode;
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const InjectorType injectorType = controls.injector_type;
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const auto& pu = baseif_.phaseUsage();
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const double efficiencyFactor = baseif_.wellEcl().getEfficiencyFactor();
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switch (current) {
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case Well::InjectorCMode::RATE: {
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control_eq = injection_rate - controls.surface_rate;
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break;
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}
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case Well::InjectorCMode::RESV: {
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std::vector<double> convert_coeff(baseif_.numPhases(), 1.0);
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baseif_.rateConverter().calcInjCoeff(/*fipreg*/ 0, baseif_.pvtRegionIdx(), convert_coeff);
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double coeff = 1.0;
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switch (injectorType) {
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case InjectorType::WATER: {
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coeff = convert_coeff[pu.phase_pos[BlackoilPhases::Aqua]];
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break;
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}
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case InjectorType::OIL: {
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coeff = convert_coeff[pu.phase_pos[BlackoilPhases::Liquid]];
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break;
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}
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case InjectorType::GAS: {
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coeff = convert_coeff[pu.phase_pos[BlackoilPhases::Vapour]];
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break;
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}
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default:
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throw("Expected WATER, OIL or GAS as type for injectors " + baseif_.wellEcl().name());
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}
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control_eq = coeff * injection_rate - controls.reservoir_rate;
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break;
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}
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case Well::InjectorCMode::THP: {
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control_eq = bhp - bhp_from_thp();
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break;
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}
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case Well::InjectorCMode::BHP: {
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control_eq = bhp - controls.bhp_limit;
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break;
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}
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case Well::InjectorCMode::GRUP: {
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assert(baseif_.wellEcl().isAvailableForGroupControl());
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const auto& group = schedule.getGroup(baseif_.wellEcl().groupName(), baseif_.currentStep());
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this->getGroupInjectionControl(group,
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well_state,
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group_state,
|
|
schedule,
|
|
summaryState,
|
|
injectorType,
|
|
bhp,
|
|
injection_rate,
|
|
control_eq,
|
|
efficiencyFactor,
|
|
deferred_logger);
|
|
break;
|
|
}
|
|
case Well::InjectorCMode::CMODE_UNDEFINED: {
|
|
OPM_DEFLOG_THROW(std::runtime_error, "Well control must be specified for well " + baseif_.name(), deferred_logger);
|
|
}
|
|
}
|
|
}
|
|
|
|
template<class FluidSystem>
|
|
template<class EvalWell>
|
|
EvalWell
|
|
WellInterfaceEval<FluidSystem>::
|
|
calculateBhpFromThp(const WellState& well_state,
|
|
const std::vector<EvalWell>& rates,
|
|
const Well& well,
|
|
const SummaryState& summaryState,
|
|
const double rho,
|
|
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 EvalWell aqua = rates[Water];
|
|
const EvalWell liquid = rates[Oil];
|
|
const EvalWell vapour = rates[Gas];
|
|
|
|
// pick the reference density
|
|
// typically the reference in the top layer
|
|
if (baseif_.isInjector() )
|
|
{
|
|
const auto& controls = well.injectionControls(summaryState);
|
|
const double vfp_ref_depth = baseif_.vfpProperties()->getInj()->getTable(controls.vfp_table_number).getDatumDepth();
|
|
const double dp = wellhelpers::computeHydrostaticCorrection(baseif_.refDepth(), vfp_ref_depth, rho, baseif_.gravity());
|
|
return baseif_.vfpProperties()->getInj()->bhp(controls.vfp_table_number, aqua, liquid, vapour, baseif_.getTHPConstraint(summaryState)) - dp;
|
|
}
|
|
else if (baseif_.isProducer()) {
|
|
const auto& controls = well.productionControls(summaryState);
|
|
const double vfp_ref_depth = baseif_.vfpProperties()->getProd()->getTable(controls.vfp_table_number).getDatumDepth();
|
|
const double dp = wellhelpers::computeHydrostaticCorrection(baseif_.refDepth(), vfp_ref_depth, rho, baseif_.gravity());
|
|
return baseif_.vfpProperties()->getProd()->bhp(controls.vfp_table_number, aqua, liquid, vapour, baseif_.getTHPConstraint(summaryState), baseif_.getALQ(well_state)) - dp;
|
|
}
|
|
else {
|
|
OPM_DEFLOG_THROW(std::logic_error, "Expected INJECTOR or PRODUCER for well " + baseif_.name(), deferred_logger);
|
|
}
|
|
}
|
|
|
|
#define INSTANCE_METHODS(A,...) \
|
|
template void WellInterfaceEval<A>:: \
|
|
assembleControlEqProd_<__VA_ARGS__>(const WellState&, \
|
|
const GroupState&, \
|
|
const Schedule&, \
|
|
const SummaryState&, \
|
|
const Well::ProductionControls&, \
|
|
const __VA_ARGS__&, \
|
|
const std::vector<__VA_ARGS__>&, \
|
|
const std::function<__VA_ARGS__()>&, \
|
|
__VA_ARGS__&, \
|
|
DeferredLogger&) const; \
|
|
template void WellInterfaceEval<A>:: \
|
|
assembleControlEqInj_<__VA_ARGS__>(const WellState&, \
|
|
const GroupState&, \
|
|
const Schedule&, \
|
|
const SummaryState&, \
|
|
const Well::InjectionControls&, \
|
|
const __VA_ARGS__&, \
|
|
const __VA_ARGS__&, \
|
|
const std::function<__VA_ARGS__()>&, \
|
|
__VA_ARGS__&, \
|
|
DeferredLogger&) const; \
|
|
template __VA_ARGS__ WellInterfaceEval<A>:: \
|
|
calculateBhpFromThp<__VA_ARGS__>(const WellState&, \
|
|
const std::vector<__VA_ARGS__>&, \
|
|
const Well&, \
|
|
const SummaryState&, \
|
|
const double, \
|
|
DeferredLogger&) const;
|
|
|
|
using FluidSys = BlackOilFluidSystem<double, BlackOilDefaultIndexTraits>;
|
|
|
|
template class WellInterfaceEval<FluidSys>;
|
|
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,3,0u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,4,0u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,5,0u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,6,0u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,7,0u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,8,0u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,-1,4u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,-1,5u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,-1,6u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,-1,7u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,-1,8u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,-1,9u>)
|
|
INSTANCE_METHODS(FluidSys, DenseAd::Evaluation<double,-1,10u>)
|
|
|
|
#define INSTANCE_BHP(...) \
|
|
template double WellInterfaceEval<__VA_ARGS__>:: \
|
|
calculateBhpFromThp<double>(const WellState&, \
|
|
const std::vector<double>&, \
|
|
const Well&, \
|
|
const SummaryState&, \
|
|
const double, \
|
|
DeferredLogger&) const;
|
|
|
|
INSTANCE_BHP(FluidSys)
|
|
|
|
} // namespace Opm
|