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68f9180a65
Using &stdwells.wells() throws an assertion for null pointers without -DNDEBUG, but was used nevertheless. That prevented running models without wells.
1246 lines
47 KiB
C++
1246 lines
47 KiB
C++
/*
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Copyright 2016 SINTEF ICT, Applied Mathematics.
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Copyright 2016 Statoil ASA.
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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/autodiff/StandardWells.hpp>
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#include <opm/autodiff/WellDensitySegmented.hpp>
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#include <opm/autodiff/VFPInjProperties.hpp>
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#include <opm/autodiff/VFPProdProperties.hpp>
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#include <opm/autodiff/WellHelpers.hpp>
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namespace Opm
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{
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StandardWells::
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WellOps::WellOps(const Wells* wells)
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: w2p(),
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p2w(),
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well_cells()
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{
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if( wells )
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{
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w2p = Eigen::SparseMatrix<double>(wells->well_connpos[ wells->number_of_wells ], wells->number_of_wells);
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p2w = Eigen::SparseMatrix<double>(wells->number_of_wells, wells->well_connpos[ wells->number_of_wells ]);
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const int nw = wells->number_of_wells;
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const int* const wpos = wells->well_connpos;
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typedef Eigen::Triplet<double> Tri;
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std::vector<Tri> scatter, gather;
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scatter.reserve(wpos[nw]);
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gather .reserve(wpos[nw]);
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for (int w = 0, i = 0; w < nw; ++w) {
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for (; i < wpos[ w + 1 ]; ++i) {
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scatter.push_back(Tri(i, w, 1.0));
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gather .push_back(Tri(w, i, 1.0));
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}
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}
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w2p.setFromTriplets(scatter.begin(), scatter.end());
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p2w.setFromTriplets(gather .begin(), gather .end());
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well_cells.assign(wells->well_cells, wells->well_cells + wells->well_connpos[wells->number_of_wells]);
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}
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}
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StandardWells::StandardWells(const Wells* wells_arg)
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: wells_(wells_arg)
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, wops_(wells_arg)
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, fluid_(nullptr)
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, active_(nullptr)
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, phase_condition_(nullptr)
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, vfp_properties_(nullptr)
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, well_perforation_densities_(Vector())
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, well_perforation_pressure_diffs_(Vector())
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, store_well_perforation_fluxes_(false)
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{
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}
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void
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StandardWells::init(const BlackoilPropsAdInterface* fluid_arg,
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const std::vector<bool>* active_arg,
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const std::vector<PhasePresence>* pc_arg,
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const VFPProperties* vfp_properties_arg,
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const double gravity_arg,
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const Vector& depth_arg)
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{
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fluid_ = fluid_arg;
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active_ = active_arg;
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phase_condition_ = pc_arg;
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vfp_properties_ = vfp_properties_arg;
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gravity_ = gravity_arg;
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perf_cell_depth_ = subset(depth_arg, wellOps().well_cells);;
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}
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const Wells& StandardWells::wells() const
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{
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assert(wells_ != 0);
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return *(wells_);
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}
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const Wells* StandardWells::wellsPointer() const
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{
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return wells_;
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}
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bool StandardWells::wellsActive() const
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{
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return wells_active_;
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}
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void StandardWells::setWellsActive(const bool wells_active)
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{
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wells_active_ = wells_active;
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}
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bool StandardWells::localWellsActive() const
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{
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return wells_ ? (wells_->number_of_wells > 0 ) : false;
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}
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int
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StandardWells::numWellVars() const
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{
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// For each well, we have a bhp variable, and one flux per phase.
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const int nw = localWellsActive() ? wells().number_of_wells : 0;
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return (numPhases() + 1) * nw;
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}
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const StandardWells::WellOps&
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StandardWells::wellOps() const
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{
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return wops_;
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}
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StandardWells::Vector& StandardWells::wellPerforationDensities()
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{
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return well_perforation_densities_;
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}
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const StandardWells::Vector&
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StandardWells::wellPerforationDensities() const
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{
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return well_perforation_densities_;
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}
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StandardWells::Vector&
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StandardWells::wellPerforationPressureDiffs()
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{
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return well_perforation_pressure_diffs_;
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}
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const StandardWells::Vector&
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StandardWells::wellPerforationPressureDiffs() const
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{
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return well_perforation_pressure_diffs_;
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}
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template<class SolutionState, class WellState>
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void
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StandardWells::
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computePropertiesForWellConnectionPressures(const SolutionState& state,
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const WellState& xw,
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std::vector<double>& b_perf,
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std::vector<double>& rsmax_perf,
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std::vector<double>& rvmax_perf,
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std::vector<double>& surf_dens_perf)
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{
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const int nperf = wells().well_connpos[wells().number_of_wells];
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const int nw = wells().number_of_wells;
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// Compute the average pressure in each well block
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const Vector perf_press = Eigen::Map<const Vector>(xw.perfPress().data(), nperf);
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Vector avg_press = perf_press*0;
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for (int w = 0; w < nw; ++w) {
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for (int perf = wells().well_connpos[w]; perf < wells().well_connpos[w+1]; ++perf) {
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const double p_above = perf == wells().well_connpos[w] ? state.bhp.value()[w] : perf_press[perf - 1];
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const double p_avg = (perf_press[perf] + p_above)/2;
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avg_press[perf] = p_avg;
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}
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}
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const std::vector<int>& well_cells = wellOps().well_cells;
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// Use cell values for the temperature as the wells don't knows its temperature yet.
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const ADB perf_temp = subset(state.temperature, well_cells);
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// Compute b, rsmax, rvmax values for perforations.
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// Evaluate the properties using average well block pressures
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// and cell values for rs, rv, phase condition and temperature.
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const ADB avg_press_ad = ADB::constant(avg_press);
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std::vector<PhasePresence> perf_cond(nperf);
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// const std::vector<PhasePresence>& pc = phaseCondition();
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for (int perf = 0; perf < nperf; ++perf) {
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perf_cond[perf] = (*phase_condition_)[well_cells[perf]];
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}
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const PhaseUsage& pu = fluid_->phaseUsage();
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DataBlock b(nperf, pu.num_phases);
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if (pu.phase_used[BlackoilPhases::Aqua]) {
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const Vector bw = fluid_->bWat(avg_press_ad, perf_temp, well_cells).value();
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b.col(pu.phase_pos[BlackoilPhases::Aqua]) = bw;
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}
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assert((*active_)[Oil]);
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const Vector perf_so = subset(state.saturation[pu.phase_pos[Oil]].value(), well_cells);
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if (pu.phase_used[BlackoilPhases::Liquid]) {
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const ADB perf_rs = (state.rs.size() > 0) ? subset(state.rs, well_cells) : ADB::null();
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const Vector bo = fluid_->bOil(avg_press_ad, perf_temp, perf_rs, perf_cond, well_cells).value();
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b.col(pu.phase_pos[BlackoilPhases::Liquid]) = bo;
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}
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if (pu.phase_used[BlackoilPhases::Vapour]) {
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const ADB perf_rv = (state.rv.size() > 0) ? subset(state.rv, well_cells) : ADB::null();
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const Vector bg = fluid_->bGas(avg_press_ad, perf_temp, perf_rv, perf_cond, well_cells).value();
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b.col(pu.phase_pos[BlackoilPhases::Vapour]) = bg;
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}
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if (pu.phase_used[BlackoilPhases::Liquid] && pu.phase_used[BlackoilPhases::Vapour]) {
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const Vector rssat = fluid_->rsSat(ADB::constant(avg_press), ADB::constant(perf_so), well_cells).value();
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rsmax_perf.assign(rssat.data(), rssat.data() + nperf);
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const Vector rvsat = fluid_->rvSat(ADB::constant(avg_press), ADB::constant(perf_so), well_cells).value();
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rvmax_perf.assign(rvsat.data(), rvsat.data() + nperf);
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}
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// b is row major, so can just copy data.
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b_perf.assign(b.data(), b.data() + nperf * pu.num_phases);
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// Surface density.
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// The compute density segment wants the surface densities as
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// an np * number of wells cells array
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Vector rho = superset(fluid_->surfaceDensity(0 , well_cells), Span(nperf, pu.num_phases, 0), nperf*pu.num_phases);
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for (int phase = 1; phase < pu.num_phases; ++phase) {
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rho += superset(fluid_->surfaceDensity(phase , well_cells), Span(nperf, pu.num_phases, phase), nperf*pu.num_phases);
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}
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surf_dens_perf.assign(rho.data(), rho.data() + nperf * pu.num_phases);
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}
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template <class WellState>
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void
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StandardWells::
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computeWellConnectionDensitesPressures(const WellState& xw,
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const std::vector<double>& b_perf,
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const std::vector<double>& rsmax_perf,
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const std::vector<double>& rvmax_perf,
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const std::vector<double>& surf_dens_perf,
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const std::vector<double>& depth_perf,
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const double grav)
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{
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// Compute densities
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std::vector<double> cd =
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WellDensitySegmented::computeConnectionDensities(
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wells(), xw, fluid_->phaseUsage(),
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b_perf, rsmax_perf, rvmax_perf, surf_dens_perf);
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const int nperf = wells().well_connpos[wells().number_of_wells];
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// Compute pressure deltas
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std::vector<double> cdp =
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WellDensitySegmented::computeConnectionPressureDelta(
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wells(), depth_perf, cd, grav);
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// Store the results
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well_perforation_densities_ = Eigen::Map<const Vector>(cd.data(), nperf);
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well_perforation_pressure_diffs_ = Eigen::Map<const Vector>(cdp.data(), nperf);
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}
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template <class SolutionState, class WellState>
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void
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StandardWells::
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computeWellConnectionPressures(const SolutionState& state,
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const WellState& xw)
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{
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if( ! localWellsActive() ) return ;
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// 1. Compute properties required by computeConnectionPressureDelta().
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// Note that some of the complexity of this part is due to the function
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// taking std::vector<double> arguments, and not Eigen objects.
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std::vector<double> b_perf;
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std::vector<double> rsmax_perf;
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std::vector<double> rvmax_perf;
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std::vector<double> surf_dens_perf;
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computePropertiesForWellConnectionPressures(state, xw, b_perf, rsmax_perf, rvmax_perf, surf_dens_perf);
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const Vector& pdepth = perf_cell_depth_;
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const int nperf = wells().well_connpos[wells().number_of_wells];
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const std::vector<double> depth_perf(pdepth.data(), pdepth.data() + nperf);
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computeWellConnectionDensitesPressures(xw, b_perf, rsmax_perf, rvmax_perf, surf_dens_perf, depth_perf, gravity_);
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}
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template <class ReservoirResidualQuant, class SolutionState>
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void
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StandardWells::
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extractWellPerfProperties(const SolutionState& /* state */,
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const std::vector<ReservoirResidualQuant>& rq,
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std::vector<ADB>& mob_perfcells,
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std::vector<ADB>& b_perfcells) const
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{
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// If we have wells, extract the mobilities and b-factors for
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// the well-perforated cells.
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if ( !localWellsActive() ) {
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mob_perfcells.clear();
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b_perfcells.clear();
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return;
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} else {
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const std::vector<int>& well_cells = wellOps().well_cells;
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const int num_phases_ = wells().number_of_phases;
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mob_perfcells.resize(num_phases_, ADB::null());
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b_perfcells.resize(num_phases_, ADB::null());
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for (int phase = 0; phase < num_phases_; ++phase) {
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mob_perfcells[phase] = subset(rq[phase].mob, well_cells);
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b_perfcells[phase] = subset(rq[phase].b, well_cells);
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}
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}
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}
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template <class SolutionState>
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void
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StandardWells::
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computeWellFlux(const SolutionState& state,
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const std::vector<ADB>& mob_perfcells,
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const std::vector<ADB>& b_perfcells,
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Vector& aliveWells,
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std::vector<ADB>& cq_s) const
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{
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if( ! localWellsActive() ) return ;
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const int np = wells().number_of_phases;
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const int nw = wells().number_of_wells;
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const int nperf = wells().well_connpos[nw];
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Vector Tw = Eigen::Map<const Vector>(wells().WI, nperf);
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const std::vector<int>& well_cells = wellOps().well_cells;
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// pressure diffs computed already (once per step, not changing per iteration)
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const Vector& cdp = wellPerforationPressureDiffs();
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// Extract needed quantities for the perforation cells
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const ADB& p_perfcells = subset(state.pressure, well_cells);
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// Perforation pressure
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const ADB perfpressure = (wellOps().w2p * state.bhp) + cdp;
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// Pressure drawdown (also used to determine direction of flow)
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const ADB drawdown = p_perfcells - perfpressure;
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// Compute vectors with zero and ones that
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// selects the wanted quantities.
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// selects injection perforations
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Vector selectInjectingPerforations = Vector::Zero(nperf);
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// selects producing perforations
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Vector selectProducingPerforations = Vector::Zero(nperf);
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for (int c = 0; c < nperf; ++c){
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if (drawdown.value()[c] < 0)
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selectInjectingPerforations[c] = 1;
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else
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selectProducingPerforations[c] = 1;
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}
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// Handle cross flow
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const Vector numInjectingPerforations = (wellOps().p2w * ADB::constant(selectInjectingPerforations)).value();
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const Vector numProducingPerforations = (wellOps().p2w * ADB::constant(selectProducingPerforations)).value();
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for (int w = 0; w < nw; ++w) {
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if (!wells().allow_cf[w]) {
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for (int perf = wells().well_connpos[w] ; perf < wells().well_connpos[w+1]; ++perf) {
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// Crossflow is not allowed; reverse flow is prevented.
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// At least one of the perforation must be open in order to have a meeningful
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// equation to solve. For the special case where all perforations have reverse flow,
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// and the target rate is non-zero all of the perforations are keept open.
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if (wells().type[w] == INJECTOR && numInjectingPerforations[w] > 0) {
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selectProducingPerforations[perf] = 0.0;
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} else if (wells().type[w] == PRODUCER && numProducingPerforations[w] > 0 ){
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selectInjectingPerforations[perf] = 0.0;
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}
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}
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}
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}
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// HANDLE FLOW INTO WELLBORE
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// compute phase volumetric rates at standard conditions
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std::vector<ADB> cq_p(np, ADB::null());
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std::vector<ADB> cq_ps(np, ADB::null());
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for (int phase = 0; phase < np; ++phase) {
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cq_p[phase] = -(selectProducingPerforations * Tw) * (mob_perfcells[phase] * drawdown);
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cq_ps[phase] = b_perfcells[phase] * cq_p[phase];
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}
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const Opm::PhaseUsage& pu = fluid_->phaseUsage();
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if ((*active_)[Oil] && (*active_)[Gas]) {
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const int oilpos = pu.phase_pos[Oil];
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const int gaspos = pu.phase_pos[Gas];
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const ADB cq_psOil = cq_ps[oilpos];
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const ADB cq_psGas = cq_ps[gaspos];
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const ADB& rv_perfcells = subset(state.rv, well_cells);
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const ADB& rs_perfcells = subset(state.rs, well_cells);
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cq_ps[gaspos] += rs_perfcells * cq_psOil;
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cq_ps[oilpos] += rv_perfcells * cq_psGas;
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}
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// HANDLE FLOW OUT FROM WELLBORE
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// Using total mobilities
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ADB total_mob = mob_perfcells[0];
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for (int phase = 1; phase < np; ++phase) {
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total_mob += mob_perfcells[phase];
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}
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// injection perforations total volume rates
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const ADB cqt_i = -(selectInjectingPerforations * Tw) * (total_mob * drawdown);
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// Store well perforation total fluxes (reservor volumes) if requested.
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if (store_well_perforation_fluxes_) {
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// Ugly const-cast, but unappealing alternatives.
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Vector& wf = const_cast<Vector&>(well_perforation_fluxes_);
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wf = cqt_i.value();
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for (int phase = 0; phase < np; ++phase) {
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wf += cq_p[phase].value();
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}
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}
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// compute wellbore mixture for injecting perforations
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// The wellbore mixture depends on the inflow from the reservoar
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// and the well injection rates.
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// compute avg. and total wellbore phase volumetric rates at standard conds
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const DataBlock compi = Eigen::Map<const DataBlock>(wells().comp_frac, nw, np);
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std::vector<ADB> wbq(np, ADB::null());
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ADB wbqt = ADB::constant(Vector::Zero(nw));
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for (int phase = 0; phase < np; ++phase) {
|
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const ADB& q_ps = wellOps().p2w * cq_ps[phase];
|
|
const ADB& q_s = subset(state.qs, Span(nw, 1, phase*nw));
|
|
Selector<double> injectingPhase_selector(q_s.value(), Selector<double>::GreaterZero);
|
|
const int pos = pu.phase_pos[phase];
|
|
wbq[phase] = (compi.col(pos) * injectingPhase_selector.select(q_s,ADB::constant(Vector::Zero(nw)))) - q_ps;
|
|
wbqt += wbq[phase];
|
|
}
|
|
// compute wellbore mixture at standard conditions.
|
|
Selector<double> notDeadWells_selector(wbqt.value(), Selector<double>::Zero);
|
|
std::vector<ADB> cmix_s(np, ADB::null());
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
const int pos = pu.phase_pos[phase];
|
|
cmix_s[phase] = wellOps().w2p * notDeadWells_selector.select(ADB::constant(compi.col(pos)), wbq[phase]/wbqt);
|
|
}
|
|
|
|
// compute volume ratio between connection at standard conditions
|
|
ADB volumeRatio = ADB::constant(Vector::Zero(nperf));
|
|
|
|
if ((*active_)[Water]) {
|
|
const int watpos = pu.phase_pos[Water];
|
|
volumeRatio += cmix_s[watpos] / b_perfcells[watpos];
|
|
}
|
|
|
|
if ((*active_)[Oil] && (*active_)[Gas]) {
|
|
// Incorporate RS/RV factors if both oil and gas active
|
|
const ADB& rv_perfcells = subset(state.rv, well_cells);
|
|
const ADB& rs_perfcells = subset(state.rs, well_cells);
|
|
const ADB d = Vector::Constant(nperf,1.0) - rv_perfcells * rs_perfcells;
|
|
|
|
const int oilpos = pu.phase_pos[Oil];
|
|
const int gaspos = pu.phase_pos[Gas];
|
|
|
|
const ADB tmp_oil = (cmix_s[oilpos] - rv_perfcells * cmix_s[gaspos]) / d;
|
|
volumeRatio += tmp_oil / b_perfcells[oilpos];
|
|
|
|
const ADB tmp_gas = (cmix_s[gaspos] - rs_perfcells * cmix_s[oilpos]) / d;
|
|
volumeRatio += tmp_gas / b_perfcells[gaspos];
|
|
}
|
|
else {
|
|
if ((*active_)[Oil]) {
|
|
const int oilpos = pu.phase_pos[Oil];
|
|
volumeRatio += cmix_s[oilpos] / b_perfcells[oilpos];
|
|
}
|
|
if ((*active_)[Gas]) {
|
|
const int gaspos = pu.phase_pos[Gas];
|
|
volumeRatio += cmix_s[gaspos] / b_perfcells[gaspos];
|
|
}
|
|
}
|
|
|
|
|
|
// injecting connections total volumerates at standard conditions
|
|
ADB cqt_is = cqt_i/volumeRatio;
|
|
|
|
// connection phase volumerates at standard conditions
|
|
cq_s.resize(np, ADB::null());
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
cq_s[phase] = cq_ps[phase] + cmix_s[phase]*cqt_is;
|
|
}
|
|
|
|
// check for dead wells (used in the well controll equations)
|
|
aliveWells = Vector::Constant(nw, 1.0);
|
|
for (int w = 0; w < nw; ++w) {
|
|
if (wbqt.value()[w] == 0) {
|
|
aliveWells[w] = 0.0;
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <class SolutionState, class WellState>
|
|
void
|
|
StandardWells::
|
|
updatePerfPhaseRatesAndPressures(const std::vector<ADB>& cq_s,
|
|
const SolutionState& state,
|
|
WellState& xw) const
|
|
{
|
|
if ( !localWellsActive() )
|
|
{
|
|
// If there are no wells in the subdomain of the proces then
|
|
// cq_s has zero size and will cause a segmentation fault below.
|
|
return;
|
|
}
|
|
|
|
// Update the perforation phase rates (used to calculate the pressure drop in the wellbore).
|
|
const int np = wells().number_of_phases;
|
|
const int nw = wells().number_of_wells;
|
|
const int nperf = wells().well_connpos[nw];
|
|
Vector cq = superset(cq_s[0].value(), Span(nperf, np, 0), nperf*np);
|
|
for (int phase = 1; phase < np; ++phase) {
|
|
cq += superset(cq_s[phase].value(), Span(nperf, np, phase), nperf*np);
|
|
}
|
|
xw.perfPhaseRates().assign(cq.data(), cq.data() + nperf*np);
|
|
|
|
// Update the perforation pressures.
|
|
const Vector& cdp = wellPerforationPressureDiffs();
|
|
const Vector perfpressure = (wellOps().w2p * state.bhp.value().matrix()).array() + cdp;
|
|
xw.perfPress().assign(perfpressure.data(), perfpressure.data() + nperf);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <class WellState>
|
|
void
|
|
StandardWells::
|
|
updateWellState(const Vector& dwells,
|
|
const double dpmaxrel,
|
|
WellState& well_state)
|
|
{
|
|
if( localWellsActive() )
|
|
{
|
|
const int np = wells().number_of_phases;
|
|
const int nw = wells().number_of_wells;
|
|
|
|
// Extract parts of dwells corresponding to each part.
|
|
int varstart = 0;
|
|
const Vector dqs = subset(dwells, Span(np*nw, 1, varstart));
|
|
varstart += dqs.size();
|
|
const Vector dbhp = subset(dwells, Span(nw, 1, varstart));
|
|
varstart += dbhp.size();
|
|
assert(varstart == dwells.size());
|
|
|
|
|
|
// Qs update.
|
|
// Since we need to update the wellrates, that are ordered by wells,
|
|
// from dqs which are ordered by phase, the simplest is to compute
|
|
// dwr, which is the data from dqs but ordered by wells.
|
|
const DataBlock wwr = Eigen::Map<const DataBlock>(dqs.data(), np, nw).transpose();
|
|
const Vector dwr = Eigen::Map<const Vector>(wwr.data(), nw*np);
|
|
const Vector wr_old = Eigen::Map<const Vector>(&well_state.wellRates()[0], nw*np);
|
|
const Vector wr = wr_old - dwr;
|
|
std::copy(&wr[0], &wr[0] + wr.size(), well_state.wellRates().begin());
|
|
|
|
// Bhp update.
|
|
const Vector bhp_old = Eigen::Map<const Vector>(&well_state.bhp()[0], nw, 1);
|
|
const Vector dbhp_limited = sign(dbhp) * dbhp.abs().min(bhp_old.abs()*dpmaxrel);
|
|
const Vector bhp = bhp_old - dbhp_limited;
|
|
std::copy(&bhp[0], &bhp[0] + bhp.size(), well_state.bhp().begin());
|
|
|
|
|
|
const Opm::PhaseUsage& pu = fluid_->phaseUsage();
|
|
//Loop over all wells
|
|
#pragma omp parallel for schedule(static)
|
|
for (int w = 0; w < nw; ++w) {
|
|
const WellControls* wc = wells().ctrls[w];
|
|
const int nwc = well_controls_get_num(wc);
|
|
//Loop over all controls until we find a THP control
|
|
//that specifies what we need...
|
|
//Will only update THP for wells with THP control
|
|
for (int ctrl_index=0; ctrl_index < nwc; ++ctrl_index) {
|
|
if (well_controls_iget_type(wc, ctrl_index) == THP) {
|
|
double aqua = 0.0;
|
|
double liquid = 0.0;
|
|
double vapour = 0.0;
|
|
|
|
if ((*active_)[ Water ]) {
|
|
aqua = wr[w*np + pu.phase_pos[ Water ] ];
|
|
}
|
|
if ((*active_)[ Oil ]) {
|
|
liquid = wr[w*np + pu.phase_pos[ Oil ] ];
|
|
}
|
|
if ((*active_)[ Gas ]) {
|
|
vapour = wr[w*np + pu.phase_pos[ Gas ] ];
|
|
}
|
|
|
|
double alq = well_controls_iget_alq(wc, ctrl_index);
|
|
int table_id = well_controls_iget_vfp(wc, ctrl_index);
|
|
|
|
const WellType& well_type = wells().type[w];
|
|
if (well_type == INJECTOR) {
|
|
double dp = wellhelpers::computeHydrostaticCorrection(
|
|
wells(), w, vfp_properties_->getInj()->getTable(table_id)->getDatumDepth(),
|
|
wellPerforationDensities(), gravity_);
|
|
|
|
well_state.thp()[w] = vfp_properties_->getInj()->thp(table_id, aqua, liquid, vapour, bhp[w] + dp);
|
|
}
|
|
else if (well_type == PRODUCER) {
|
|
double dp = wellhelpers::computeHydrostaticCorrection(
|
|
wells(), w, vfp_properties_->getProd()->getTable(table_id)->getDatumDepth(),
|
|
wellPerforationDensities(), gravity_);
|
|
|
|
well_state.thp()[w] = vfp_properties_->getProd()->thp(table_id, aqua, liquid, vapour, bhp[w] + dp, alq);
|
|
}
|
|
else {
|
|
OPM_THROW(std::logic_error, "Expected INJECTOR or PRODUCER well");
|
|
}
|
|
|
|
//Assume only one THP control specified for each well
|
|
break;
|
|
}
|
|
}
|
|
}
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <class WellState>
|
|
void
|
|
StandardWells::
|
|
updateWellControls(WellState& xw) const
|
|
{
|
|
if( !localWellsActive() ) return ;
|
|
|
|
std::string modestring[4] = { "BHP", "THP", "RESERVOIR_RATE", "SURFACE_RATE" };
|
|
// Find, for each well, if any constraints are broken. If so,
|
|
// switch control to first broken constraint.
|
|
const int np = wells().number_of_phases;
|
|
const int nw = wells().number_of_wells;
|
|
#pragma omp parallel for schedule(dynamic)
|
|
for (int w = 0; w < nw; ++w) {
|
|
const WellControls* wc = wells().ctrls[w];
|
|
// The current control in the well state overrides
|
|
// the current control set in the Wells struct, which
|
|
// is instead treated as a default.
|
|
int current = xw.currentControls()[w];
|
|
// Loop over all controls except the current one, and also
|
|
// skip any RESERVOIR_RATE controls, since we cannot
|
|
// handle those.
|
|
const int nwc = well_controls_get_num(wc);
|
|
int ctrl_index = 0;
|
|
for (; ctrl_index < nwc; ++ctrl_index) {
|
|
if (ctrl_index == current) {
|
|
// This is the currently used control, so it is
|
|
// used as an equation. So this is not used as an
|
|
// inequality constraint, and therefore skipped.
|
|
continue;
|
|
}
|
|
if (wellhelpers::constraintBroken(
|
|
xw.bhp(), xw.thp(), xw.wellRates(),
|
|
w, np, wells().type[w], wc, ctrl_index)) {
|
|
// ctrl_index will be the index of the broken constraint after the loop.
|
|
break;
|
|
}
|
|
}
|
|
if (ctrl_index != nwc) {
|
|
// Constraint number ctrl_index was broken, switch to it.
|
|
// We disregard terminal_ouput here as with it only messages
|
|
// for wells on one process will be printed.
|
|
std::ostringstream ss;
|
|
ss << "Switching control mode for well " << wells().name[w]
|
|
<< " from " << modestring[well_controls_iget_type(wc, current)]
|
|
<< " to " << modestring[well_controls_iget_type(wc, ctrl_index)] << std::endl;
|
|
OpmLog::info(ss.str());
|
|
xw.currentControls()[w] = ctrl_index;
|
|
current = xw.currentControls()[w];
|
|
}
|
|
|
|
// 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:
|
|
xw.bhp()[w] = target;
|
|
break;
|
|
|
|
case THP: {
|
|
double aqua = 0.0;
|
|
double liquid = 0.0;
|
|
double vapour = 0.0;
|
|
|
|
const Opm::PhaseUsage& pu = fluid_->phaseUsage();
|
|
|
|
if ((*active_)[ Water ]) {
|
|
aqua = xw.wellRates()[w*np + pu.phase_pos[ Water ] ];
|
|
}
|
|
if ((*active_)[ Oil ]) {
|
|
liquid = xw.wellRates()[w*np + pu.phase_pos[ Oil ] ];
|
|
}
|
|
if ((*active_)[ Gas ]) {
|
|
vapour = xw.wellRates()[w*np + pu.phase_pos[ Gas ] ];
|
|
}
|
|
|
|
const int vfp = well_controls_iget_vfp(wc, current);
|
|
const double& thp = well_controls_iget_target(wc, current);
|
|
const double& alq = well_controls_iget_alq(wc, current);
|
|
|
|
//Set *BHP* target by calculating bhp from THP
|
|
const WellType& well_type = wells().type[w];
|
|
|
|
if (well_type == INJECTOR) {
|
|
double dp = wellhelpers::computeHydrostaticCorrection(
|
|
wells(), w, vfp_properties_->getInj()->getTable(vfp)->getDatumDepth(),
|
|
wellPerforationDensities(), gravity_);
|
|
|
|
xw.bhp()[w] = vfp_properties_->getInj()->bhp(vfp, aqua, liquid, vapour, thp) - dp;
|
|
}
|
|
else if (well_type == PRODUCER) {
|
|
double dp = wellhelpers::computeHydrostaticCorrection(
|
|
wells(), w, vfp_properties_->getProd()->getTable(vfp)->getDatumDepth(),
|
|
wellPerforationDensities(), gravity_);
|
|
|
|
xw.bhp()[w] = vfp_properties_->getProd()->bhp(vfp, aqua, liquid, vapour, thp, alq) - dp;
|
|
}
|
|
else {
|
|
OPM_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well");
|
|
}
|
|
break;
|
|
}
|
|
|
|
case RESERVOIR_RATE:
|
|
// No direct change to any observable quantity at
|
|
// surface condition. In this case, use existing
|
|
// flow rates as initial conditions as reservoir
|
|
// rate acts only in aggregate.
|
|
break;
|
|
|
|
case SURFACE_RATE:
|
|
// assign target value as initial guess for injectors and
|
|
// single phase producers (orat, grat, wrat)
|
|
const WellType& well_type = wells().type[w];
|
|
if (well_type == INJECTOR) {
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
const double& compi = wells().comp_frac[np * w + phase];
|
|
if (compi > 0.0) {
|
|
xw.wellRates()[np*w + phase] = target * compi;
|
|
}
|
|
}
|
|
} else if (well_type == PRODUCER) {
|
|
|
|
// only set target as initial rates for single phase
|
|
// producers. (orat, grat and wrat, and not lrat)
|
|
// lrat will result in numPhasesWithTargetsUnderThisControl == 2
|
|
int numPhasesWithTargetsUnderThisControl = 0;
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
if (distr[phase] > 0.0) {
|
|
numPhasesWithTargetsUnderThisControl += 1;
|
|
}
|
|
}
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
if (distr[phase] > 0.0 && numPhasesWithTargetsUnderThisControl < 2 ) {
|
|
xw.wellRates()[np*w + phase] = target * distr[phase];
|
|
}
|
|
}
|
|
} else {
|
|
OPM_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well");
|
|
}
|
|
|
|
|
|
break;
|
|
}
|
|
}
|
|
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <class SolutionState>
|
|
void
|
|
StandardWells::
|
|
addWellFluxEq(const std::vector<ADB>& cq_s,
|
|
const SolutionState& state,
|
|
LinearisedBlackoilResidual& residual)
|
|
{
|
|
if( !localWellsActive() )
|
|
{
|
|
// If there are no wells in the subdomain of the proces then
|
|
// cq_s has zero size and will cause a segmentation fault below.
|
|
return;
|
|
}
|
|
|
|
const int np = wells().number_of_phases;
|
|
const int nw = wells().number_of_wells;
|
|
ADB qs = state.qs;
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
qs -= superset(wellOps().p2w * cq_s[phase], Span(nw, 1, phase*nw), nw*np);
|
|
|
|
}
|
|
|
|
residual.well_flux_eq = qs;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <class SolutionState, class WellState>
|
|
void
|
|
StandardWells::addWellControlEq(const SolutionState& state,
|
|
const WellState& xw,
|
|
const Vector& aliveWells,
|
|
LinearisedBlackoilResidual& residual)
|
|
{
|
|
if( ! localWellsActive() ) return;
|
|
|
|
const int np = wells().number_of_phases;
|
|
const int nw = wells().number_of_wells;
|
|
|
|
ADB aqua = ADB::constant(Vector::Zero(nw));
|
|
ADB liquid = ADB::constant(Vector::Zero(nw));
|
|
ADB vapour = ADB::constant(Vector::Zero(nw));
|
|
|
|
if ((*active_)[Water]) {
|
|
aqua += subset(state.qs, Span(nw, 1, BlackoilPhases::Aqua*nw));
|
|
}
|
|
if ((*active_)[Oil]) {
|
|
liquid += subset(state.qs, Span(nw, 1, BlackoilPhases::Liquid*nw));
|
|
}
|
|
if ((*active_)[Gas]) {
|
|
vapour += subset(state.qs, Span(nw, 1, BlackoilPhases::Vapour*nw));
|
|
}
|
|
|
|
//THP calculation variables
|
|
std::vector<int> inj_table_id(nw, -1);
|
|
std::vector<int> prod_table_id(nw, -1);
|
|
Vector thp_inj_target_v = Vector::Zero(nw);
|
|
Vector thp_prod_target_v = Vector::Zero(nw);
|
|
Vector alq_v = Vector::Zero(nw);
|
|
|
|
//Hydrostatic correction variables
|
|
Vector rho_v = Vector::Zero(nw);
|
|
Vector vfp_ref_depth_v = Vector::Zero(nw);
|
|
|
|
//Target vars
|
|
Vector bhp_targets = Vector::Zero(nw);
|
|
Vector rate_targets = Vector::Zero(nw);
|
|
Eigen::SparseMatrix<double> rate_distr(nw, np*nw);
|
|
|
|
//Selection variables
|
|
std::vector<int> bhp_elems;
|
|
std::vector<int> thp_inj_elems;
|
|
std::vector<int> thp_prod_elems;
|
|
std::vector<int> rate_elems;
|
|
|
|
//Run through all wells to calculate BHP/RATE targets
|
|
//and gather info about current control
|
|
for (int w = 0; w < nw; ++w) {
|
|
auto wc = wells().ctrls[w];
|
|
|
|
// The current control in the well state overrides
|
|
// the current control set in the Wells struct, which
|
|
// is instead treated as a default.
|
|
const int current = xw.currentControls()[w];
|
|
|
|
switch (well_controls_iget_type(wc, current)) {
|
|
case BHP:
|
|
{
|
|
bhp_elems.push_back(w);
|
|
bhp_targets(w) = well_controls_iget_target(wc, current);
|
|
rate_targets(w) = -1e100;
|
|
}
|
|
break;
|
|
|
|
case THP:
|
|
{
|
|
const int perf = wells().well_connpos[w];
|
|
rho_v[w] = wellPerforationDensities()[perf];
|
|
|
|
const int table_id = well_controls_iget_vfp(wc, current);
|
|
const double target = well_controls_iget_target(wc, current);
|
|
|
|
const WellType& well_type = wells().type[w];
|
|
if (well_type == INJECTOR) {
|
|
inj_table_id[w] = table_id;
|
|
thp_inj_target_v[w] = target;
|
|
alq_v[w] = -1e100;
|
|
|
|
vfp_ref_depth_v[w] = vfp_properties_->getInj()->getTable(table_id)->getDatumDepth();
|
|
|
|
thp_inj_elems.push_back(w);
|
|
}
|
|
else if (well_type == PRODUCER) {
|
|
prod_table_id[w] = table_id;
|
|
thp_prod_target_v[w] = target;
|
|
alq_v[w] = well_controls_iget_alq(wc, current);
|
|
|
|
vfp_ref_depth_v[w] = vfp_properties_->getProd()->getTable(table_id)->getDatumDepth();
|
|
|
|
thp_prod_elems.push_back(w);
|
|
}
|
|
else {
|
|
OPM_THROW(std::logic_error, "Expected INJECTOR or PRODUCER type well");
|
|
}
|
|
bhp_targets(w) = -1e100;
|
|
rate_targets(w) = -1e100;
|
|
}
|
|
break;
|
|
|
|
case RESERVOIR_RATE: // Intentional fall-through
|
|
case SURFACE_RATE:
|
|
{
|
|
rate_elems.push_back(w);
|
|
// RESERVOIR and SURFACE rates look the same, from a
|
|
// high-level point of view, in the system of
|
|
// simultaneous linear equations.
|
|
|
|
const double* const distr =
|
|
well_controls_iget_distr(wc, current);
|
|
|
|
for (int p = 0; p < np; ++p) {
|
|
rate_distr.insert(w, p*nw + w) = distr[p];
|
|
}
|
|
|
|
bhp_targets(w) = -1.0e100;
|
|
rate_targets(w) = well_controls_iget_target(wc, current);
|
|
}
|
|
break;
|
|
}
|
|
}
|
|
|
|
//Calculate BHP target from THP
|
|
const ADB thp_inj_target = ADB::constant(thp_inj_target_v);
|
|
const ADB thp_prod_target = ADB::constant(thp_prod_target_v);
|
|
const ADB alq = ADB::constant(alq_v);
|
|
const ADB bhp_from_thp_inj = vfp_properties_->getInj()->bhp(inj_table_id, aqua, liquid, vapour, thp_inj_target);
|
|
const ADB bhp_from_thp_prod = vfp_properties_->getProd()->bhp(prod_table_id, aqua, liquid, vapour, thp_prod_target, alq);
|
|
|
|
//Perform hydrostatic correction to computed targets
|
|
const Vector dp_v = wellhelpers::computeHydrostaticCorrection(wells(), vfp_ref_depth_v, wellPerforationDensities(), gravity_);
|
|
const ADB dp = ADB::constant(dp_v);
|
|
const ADB dp_inj = superset(subset(dp, thp_inj_elems), thp_inj_elems, nw);
|
|
const ADB dp_prod = superset(subset(dp, thp_prod_elems), thp_prod_elems, nw);
|
|
|
|
//Calculate residuals
|
|
const ADB thp_inj_residual = state.bhp - bhp_from_thp_inj + dp_inj;
|
|
const ADB thp_prod_residual = state.bhp - bhp_from_thp_prod + dp_prod;
|
|
const ADB bhp_residual = state.bhp - bhp_targets;
|
|
const ADB rate_residual = rate_distr * state.qs - rate_targets;
|
|
|
|
//Select the right residual for each well
|
|
residual.well_eq = superset(subset(bhp_residual, bhp_elems), bhp_elems, nw) +
|
|
superset(subset(thp_inj_residual, thp_inj_elems), thp_inj_elems, nw) +
|
|
superset(subset(thp_prod_residual, thp_prod_elems), thp_prod_elems, nw) +
|
|
superset(subset(rate_residual, rate_elems), rate_elems, nw);
|
|
|
|
// For wells that are dead (not flowing), and therefore not communicating
|
|
// with the reservoir, we set the equation to be equal to the well's total
|
|
// flow. This will be a solution only if the target rate is also zero.
|
|
Eigen::SparseMatrix<double> rate_summer(nw, np*nw);
|
|
for (int w = 0; w < nw; ++w) {
|
|
for (int phase = 0; phase < np; ++phase) {
|
|
rate_summer.insert(w, phase*nw + w) = 1.0;
|
|
}
|
|
}
|
|
Selector<double> alive_selector(aliveWells, Selector<double>::NotEqualZero);
|
|
residual.well_eq = alive_selector.select(residual.well_eq, rate_summer * state.qs);
|
|
// OPM_AD_DUMP(residual_.well_eq);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <class SolutionState, class WellState>
|
|
void
|
|
StandardWells::computeWellPotentials(const std::vector<ADB>& mob_perfcells,
|
|
const std::vector<ADB>& b_perfcells,
|
|
SolutionState& state0,
|
|
WellState& well_state)
|
|
{
|
|
const int nw = wells().number_of_wells;
|
|
const int np = wells().number_of_phases;
|
|
const Opm::PhaseUsage& pu = fluid_->phaseUsage();
|
|
|
|
Vector bhps = Vector::Zero(nw);
|
|
for (int w = 0; w < nw; ++w) {
|
|
const WellControls* ctrl = wells().ctrls[w];
|
|
const int nwc = well_controls_get_num(ctrl);
|
|
//Loop over all controls until we find a BHP control
|
|
//or a THP control that specifies what we need.
|
|
//Pick the value that gives the most restrictive flow
|
|
for (int ctrl_index=0; ctrl_index < nwc; ++ctrl_index) {
|
|
|
|
if (well_controls_iget_type(ctrl, ctrl_index) == BHP) {
|
|
bhps[w] = well_controls_iget_target(ctrl, ctrl_index);
|
|
}
|
|
|
|
if (well_controls_iget_type(ctrl, ctrl_index) == THP) {
|
|
double aqua = 0.0;
|
|
double liquid = 0.0;
|
|
double vapour = 0.0;
|
|
|
|
if ((*active_)[ Water ]) {
|
|
aqua = well_state.wellRates()[w*np + pu.phase_pos[ Water ] ];
|
|
}
|
|
if ((*active_)[ Oil ]) {
|
|
liquid = well_state.wellRates()[w*np + pu.phase_pos[ Oil ] ];
|
|
}
|
|
if ((*active_)[ Gas ]) {
|
|
vapour = well_state.wellRates()[w*np + pu.phase_pos[ Gas ] ];
|
|
}
|
|
|
|
const int vfp = well_controls_iget_vfp(ctrl, ctrl_index);
|
|
const double& thp = well_controls_iget_target(ctrl, ctrl_index);
|
|
const double& alq = well_controls_iget_alq(ctrl, ctrl_index);
|
|
|
|
//Set *BHP* target by calculating bhp from THP
|
|
const WellType& well_type = wells().type[w];
|
|
|
|
if (well_type == INJECTOR) {
|
|
double dp = wellhelpers::computeHydrostaticCorrection(
|
|
wells(), w, vfp_properties_->getInj()->getTable(vfp)->getDatumDepth(),
|
|
wellPerforationDensities(), gravity_);
|
|
const double bhp = vfp_properties_->getInj()->bhp(vfp, aqua, liquid, vapour, thp) - dp;
|
|
// apply the strictest of the bhp controlls i.e. smallest bhp for injectors
|
|
if ( bhp < bhps[w]) {
|
|
bhps[w] = bhp;
|
|
}
|
|
}
|
|
else if (well_type == PRODUCER) {
|
|
double dp = wellhelpers::computeHydrostaticCorrection(
|
|
wells(), w, vfp_properties_->getProd()->getTable(vfp)->getDatumDepth(),
|
|
wellPerforationDensities(), gravity_);
|
|
|
|
const double bhp = vfp_properties_->getProd()->bhp(vfp, aqua, liquid, vapour, thp, alq) - dp;
|
|
// apply the strictest of the bhp controlls i.e. largest bhp for producers
|
|
if ( bhp > bhps[w]) {
|
|
bhps[w] = bhp;
|
|
}
|
|
}
|
|
else {
|
|
OPM_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well");
|
|
}
|
|
}
|
|
}
|
|
|
|
}
|
|
|
|
// use bhp limit from control
|
|
state0.bhp = ADB::constant(bhps);
|
|
|
|
// compute well potentials
|
|
Vector aliveWells;
|
|
std::vector<ADB> well_potentials;
|
|
computeWellFlux(state0, mob_perfcells, b_perfcells, aliveWells, well_potentials);
|
|
|
|
// store well potentials in the well state
|
|
// transform to a single vector instead of separate vectors pr phase
|
|
const int nperf = wells().well_connpos[nw];
|
|
Vector cq = superset(well_potentials[0].value(), Span(nperf, np, 0), nperf*np);
|
|
for (int phase = 1; phase < np; ++phase) {
|
|
cq += superset(well_potentials[phase].value(), Span(nperf, np, phase), nperf*np);
|
|
}
|
|
well_state.wellPotentials().assign(cq.data(), cq.data() + nperf*np);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
void
|
|
StandardWells::variableStateWellIndices(std::vector<int>& indices,
|
|
int& next) const
|
|
{
|
|
indices[Qs] = next++;
|
|
indices[Bhp] = next++;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <class SolutionState>
|
|
void
|
|
StandardWells::
|
|
variableStateExtractWellsVars(const std::vector<int>& indices,
|
|
std::vector<ADB>& vars,
|
|
SolutionState& state) const
|
|
{
|
|
// Qs.
|
|
state.qs = std::move(vars[indices[Qs]]);
|
|
|
|
// Bhp.
|
|
state.bhp = std::move(vars[indices[Bhp]]);
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
std::vector<int>
|
|
StandardWells::variableWellStateIndices() const
|
|
{
|
|
// Black oil model standard is 5 equation.
|
|
// For the pure well solve, only the well equations are picked.
|
|
std::vector<int> indices(5, -1);
|
|
int next = 0;
|
|
|
|
variableStateWellIndices(indices, next);
|
|
|
|
assert(next == 2);
|
|
return indices;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
template <class WellState>
|
|
void
|
|
StandardWells::variableWellStateInitials(const WellState& xw,
|
|
std::vector<Vector>& vars0) const
|
|
{
|
|
// Initial well rates.
|
|
if ( localWellsActive() )
|
|
{
|
|
// Need to reshuffle well rates, from phase running fastest
|
|
// to wells running fastest.
|
|
const int nw = wells().number_of_wells;
|
|
const int np = wells().number_of_phases;
|
|
|
|
// The transpose() below switches the ordering.
|
|
const DataBlock wrates = Eigen::Map<const DataBlock>(& xw.wellRates()[0], nw, np).transpose();
|
|
const Vector qs = Eigen::Map<const V>(wrates.data(), nw*np);
|
|
vars0.push_back(qs);
|
|
|
|
// Initial well bottom-hole pressure.
|
|
assert (not xw.bhp().empty());
|
|
const Vector bhp = Eigen::Map<const V>(& xw.bhp()[0], xw.bhp().size());
|
|
vars0.push_back(bhp);
|
|
}
|
|
else
|
|
{
|
|
// push null states for qs and bhp
|
|
vars0.push_back(V());
|
|
vars0.push_back(V());
|
|
}
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
void
|
|
StandardWells::setStoreWellPerforationFluxesFlag(const bool store_fluxes)
|
|
{
|
|
store_well_perforation_fluxes_ = store_fluxes;
|
|
}
|
|
|
|
|
|
|
|
|
|
|
|
const StandardWells::Vector&
|
|
StandardWells::getStoredWellPerforationFluxes() const
|
|
{
|
|
assert(store_well_perforation_fluxes_);
|
|
return well_perforation_fluxes_;
|
|
}
|
|
|
|
|
|
} // namespace Opm
|