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Use extraAddWellEq() to add well contrib to polymer equation.
This way of refactoring was chosen since the extra term depends on a lot of context. Instead of recreating the context in the polymer model (which would not reduce any complexity) the necessary variables are passed to extraAddWellEq().
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@ -203,9 +203,12 @@ namespace Opm {
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assembleMassBalanceEq(const SolutionState& state);
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assembleMassBalanceEq(const SolutionState& state);
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void
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void
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addWellEq(const SolutionState& state,
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extraAddWellEq(const SolutionState& state,
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WellState& xw,
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const WellState& xw,
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V& aliveWells);
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const std::vector<ADB>& cq_ps,
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const std::vector<ADB>& cmix_s,
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const ADB& cqt_is,
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const std::vector<int>& well_cells);
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void
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void
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computeMassFlux(const int actph ,
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computeMassFlux(const int actph ,
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@ -273,176 +273,25 @@ namespace Opm {
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template <class Grid>
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template <class Grid>
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void BlackoilPolymerModel<Grid>::addWellEq(const SolutionState& state,
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void BlackoilPolymerModel<Grid>::extraAddWellEq(const SolutionState& state,
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WellState& xw,
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const WellState& xw,
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V& aliveWells)
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const std::vector<ADB>& cq_ps,
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const std::vector<ADB>& cmix_s,
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const ADB& cqt_is,
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const std::vector<int>& well_cells)
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{
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{
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if( ! wellsActive() ) return ;
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const int nc = Opm::AutoDiffGrid::numCells(grid_);
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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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const Opm::PhaseUsage& pu = fluid_.phaseUsage();
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V Tw = Eigen::Map<const V>(wells().WI, nperf);
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const std::vector<int> well_cells(wells().well_cells, wells().well_cells + nperf);
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// pressure diffs computed already (once per step, not changing per iteration)
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const V& cdp = well_perforation_pressure_diffs_;
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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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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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std::vector<ADB> mob_perfcells(np, ADB::null());
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std::vector<ADB> b_perfcells(np, ADB::null());
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for (int phase = 0; phase < np; ++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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// Perforation pressure
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const ADB perfpressure = (wops_.w2p * state.bhp) + cdp;
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std::vector<double> perfpressure_d(perfpressure.value().data(), perfpressure.value().data() + nperf);
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xw.perfPress() = perfpressure_d;
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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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V selectInjectingPerforations = V::Zero(nperf);
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// selects producing perforations
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V selectProducingPerforations = V::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 FLOW INTO WELLBORE
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// compute phase volumetric rates at standard conditions
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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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const ADB cq_p = -(selectProducingPerforations * Tw) * (mob_perfcells[phase] * drawdown);
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cq_ps[phase] = b_perfcells[phase] * cq_p;
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}
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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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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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// 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(V::Zero(nw));
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for (int phase = 0; phase < np; ++phase) {
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const ADB& q_ps = wops_.p2w * cq_ps[phase];
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const ADB& q_s = subset(state.qs, Span(nw, 1, phase*nw));
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Selector<double> injectingPhase_selector(q_s.value(), Selector<double>::GreaterZero);
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const int pos = pu.phase_pos[phase];
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wbq[phase] = (compi.col(pos) * injectingPhase_selector.select(q_s,ADB::constant(V::Zero(nw)))) - q_ps;
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wbqt += wbq[phase];
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}
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// compute wellbore mixture at standard conditions.
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Selector<double> notDeadWells_selector(wbqt.value(), Selector<double>::Zero);
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std::vector<ADB> cmix_s(np, ADB::null());
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for (int phase = 0; phase < np; ++phase) {
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const int pos = pu.phase_pos[phase];
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cmix_s[phase] = wops_.w2p * notDeadWells_selector.select(ADB::constant(compi.col(pos)), wbq[phase]/wbqt);
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}
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// compute volume ratio between connection at standard conditions
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ADB volumeRatio = ADB::constant(V::Zero(nperf));
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const ADB d = V::Constant(nperf,1.0) - rv_perfcells * rs_perfcells;
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for (int phase = 0; phase < np; ++phase) {
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ADB tmp = cmix_s[phase];
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if (phase == Oil && active_[Gas]) {
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const int gaspos = pu.phase_pos[Gas];
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tmp = tmp - rv_perfcells * cmix_s[gaspos] / d;
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}
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if (phase == Gas && active_[Oil]) {
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const int oilpos = pu.phase_pos[Oil];
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tmp = tmp - rs_perfcells * cmix_s[oilpos] / d;
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}
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volumeRatio += tmp / b_perfcells[phase];
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}
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// injecting connections total volumerates at standard conditions
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ADB cqt_is = cqt_i/volumeRatio;
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// connection phase volumerates at standard conditions
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std::vector<ADB> cq_s(np, ADB::null());
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for (int phase = 0; phase < np; ++phase) {
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cq_s[phase] = cq_ps[phase] + cmix_s[phase]*cqt_is;
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}
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// Add well contributions to mass balance equations
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for (int phase = 0; phase < np; ++phase) {
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residual_.material_balance_eq[phase] -= superset(cq_s[phase],well_cells,nc);
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}
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// Add well contributions to polymer mass balance equation
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// Add well contributions to polymer mass balance equation
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if (has_polymer_) {
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if (has_polymer_) {
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const ADB mc = computeMc(state);
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const ADB mc = computeMc(state);
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const int nc = xw.polymerInflow().size();
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const V polyin = Eigen::Map<const V>(xw.polymerInflow().data(), nc);
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const V polyin = Eigen::Map<const V>(xw.polymerInflow().data(), nc);
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const V poly_in_perf = subset(polyin, well_cells);
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const V poly_in_perf = subset(polyin, well_cells);
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const V poly_mc_perf = subset(mc, well_cells).value();
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const V poly_mc_perf = subset(mc, well_cells).value();
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residual_.material_balance_eq[poly_pos_] -= superset(cq_ps[pu.phase_pos[Water]] * poly_mc_perf
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const PhaseUsage& pu = fluid_.phaseUsage();
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+ cmix_s[pu.phase_pos[Water]] * cqt_is*poly_in_perf,
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const ADB cq_s_poly = cq_ps[pu.phase_pos[Water]] * poly_mc_perf
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well_cells, nc);
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+ cmix_s[pu.phase_pos[Water]] * cqt_is * poly_in_perf;
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residual_.material_balance_eq[poly_pos_] -= superset(cq_s_poly, well_cells, nc);
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}
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}
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// WELL EQUATIONS
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ADB qs = state.qs;
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for (int phase = 0; phase < np; ++phase) {
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qs -= superset(wops_.p2w * cq_s[phase], Span(nw, 1, phase*nw), nw*np);
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}
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// check for dead wells (used in the well controll equations)
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aliveWells = V::Constant(nw, 1.0);
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for (int w = 0; w < nw; ++w) {
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if (wbqt.value()[w] == 0) {
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aliveWells[w] = 0.0;
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}
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}
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// Update the perforation phase rates (used to calculate the pressure drop in the wellbore)
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V cq = superset(cq_s[0].value(), Span(nperf, np, 0), nperf*np);
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for (int phase = 1; phase < np; ++phase) {
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cq += superset(cq_s[phase].value(), Span(nperf, np, phase), nperf*np);
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}
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std::vector<double> cq_d(cq.data(), cq.data() + nperf*np);
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xw.perfPhaseRates() = cq_d;
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residual_.well_flux_eq = qs;
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}
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}
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