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opm-simulators/opm/autodiff/StandardWells_impl.hpp
Arne Morten Kvarving c5ae3adbbf changed: split VFP classes in base (ebos) and legacy 
to get rid of eigen usage in ebos based classes
2018-11-14 09:54:33 +01:00

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/*
Copyright 2016 SINTEF ICT, Applied Mathematics.
Copyright 2016 Statoil ASA.
This file is part of the Open Porous Media project (OPM).
OPM is free software: you can redistribute it and/or modify
it under the terms of the GNU General Public License as published by
the Free Software Foundation, either version 3 of the License, or
(at your option) any later version.
OPM is distributed in the hope that it will be useful,
but WITHOUT ANY WARRANTY; without even the implied warranty of
MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the
GNU General Public License for more details.
You should have received a copy of the GNU General Public License
along with OPM. If not, see <http://www.gnu.org/licenses/>.
*/
#include <opm/autodiff/StandardWells.hpp>
#include <opm/autodiff/WellDensitySegmented.hpp>
#include <opm/autodiff/VFPInjPropertiesLegacy.hpp>
#include <opm/autodiff/VFPProdPropertiesLegacy.hpp>
#include <opm/autodiff/WellHelpers.hpp>
namespace Opm
{
StandardWells::
WellOps::WellOps(const Wells* wells)
: w2p(),
p2w(),
well_cells()
{
if( wells )
{
w2p = Eigen::SparseMatrix<double>(wells->well_connpos[ wells->number_of_wells ], wells->number_of_wells);
p2w = Eigen::SparseMatrix<double>(wells->number_of_wells, wells->well_connpos[ wells->number_of_wells ]);
const int nw = wells->number_of_wells;
const int* const wpos = wells->well_connpos;
typedef Eigen::Triplet<double> Tri;
std::vector<Tri> scatter, gather;
scatter.reserve(wpos[nw]);
gather .reserve(wpos[nw]);
for (int w = 0, i = 0; w < nw; ++w) {
for (; i < wpos[ w + 1 ]; ++i) {
scatter.push_back(Tri(i, w, 1.0));
gather .push_back(Tri(w, i, 1.0));
}
}
w2p.setFromTriplets(scatter.begin(), scatter.end());
p2w.setFromTriplets(gather .begin(), gather .end());
well_cells.assign(wells->well_cells, wells->well_cells + wells->well_connpos[wells->number_of_wells]);
}
}
StandardWells::StandardWells(const Wells* wells_arg, WellCollection* well_collection, const int current_step)
: wells_active_(wells_arg!=nullptr)
, wells_(wells_arg)
, wops_(wells_arg)
, well_collection_(well_collection)
, current_step_(current_step)
, well_perforation_efficiency_factors_(Vector::Ones(wells_!=nullptr ? wells_->well_connpos[wells_->number_of_wells] : 0))
, fluid_(nullptr)
, active_(nullptr)
, phase_condition_(nullptr)
, vfp_properties_(nullptr)
, well_perforation_densities_(Vector())
, well_perforation_pressure_diffs_(Vector())
, store_well_perforation_fluxes_(false)
{
}
void
StandardWells::init(const BlackoilPropsAdFromDeck* fluid_arg,
const std::vector<bool>* active_arg,
const std::vector<PhasePresence>* pc_arg,
const VFPProperties<VFPInjPropertiesLegacy,VFPProdPropertiesLegacy>* vfp_properties_arg,
const double gravity_arg,
const Vector& depth_arg)
{
fluid_ = fluid_arg;
active_ = active_arg;
phase_condition_ = pc_arg;
vfp_properties_ = vfp_properties_arg;
gravity_ = gravity_arg;
perf_cell_depth_ = subset(depth_arg, wellOps().well_cells);;
calculateEfficiencyFactors();
}
const Wells& StandardWells::wells() const
{
assert(wells_ != 0);
return *(wells_);
}
const Wells* StandardWells::wellsPointer() const
{
return wells_;
}
bool StandardWells::wellsActive() const
{
return wells_active_;
}
void StandardWells::setWellsActive(const bool wells_active)
{
wells_active_ = wells_active;
}
bool StandardWells::localWellsActive() const
{
return wells_ ? (wells_->number_of_wells > 0 ) : false;
}
int
StandardWells::numWellVars() const
{
if ( !localWellsActive() )
{
return 0;
}
// For each well, we have a bhp variable, and one flux per phase.
const int nw = wells().number_of_wells;
return (numPhases() + 1) * nw;
}
const StandardWells::WellOps&
StandardWells::wellOps() const
{
return wops_;
}
StandardWells::Vector& StandardWells::wellPerforationDensities()
{
return well_perforation_densities_;
}
const StandardWells::Vector&
StandardWells::wellPerforationDensities() const
{
return well_perforation_densities_;
}
StandardWells::Vector&
StandardWells::wellPerforationPressureDiffs()
{
return well_perforation_pressure_diffs_;
}
const StandardWells::Vector&
StandardWells::wellPerforationPressureDiffs() const
{
return well_perforation_pressure_diffs_;
}
template<class SolutionState, class WellState>
void
StandardWells::
computePropertiesForWellConnectionPressures(const SolutionState& state,
const WellState& xw,
std::vector<double>& b_perf,
std::vector<double>& rsmax_perf,
std::vector<double>& rvmax_perf,
std::vector<double>& surf_dens_perf)
{
const int nperf = wells().well_connpos[wells().number_of_wells];
const int nw = wells().number_of_wells;
// Compute the average pressure in each well block
const Vector perf_press = Eigen::Map<const Vector>(xw.perfPress().data(), nperf);
Vector avg_press = perf_press*0;
for (int w = 0; w < nw; ++w) {
for (int perf = wells().well_connpos[w]; perf < wells().well_connpos[w+1]; ++perf) {
const double p_above = perf == wells().well_connpos[w] ? state.bhp.value()[w] : perf_press[perf - 1];
const double p_avg = (perf_press[perf] + p_above)/2;
avg_press[perf] = p_avg;
}
}
const std::vector<int>& well_cells = wellOps().well_cells;
// Use cell values for the temperature as the wells don't knows its temperature yet.
const ADB perf_temp = subset(state.temperature, well_cells);
// Compute b, rsmax, rvmax values for perforations.
// Evaluate the properties using average well block pressures
// and cell values for rs, rv, phase condition and temperature.
const ADB avg_press_ad = ADB::constant(avg_press);
std::vector<PhasePresence> perf_cond(nperf);
// const std::vector<PhasePresence>& pc = phaseCondition();
for (int perf = 0; perf < nperf; ++perf) {
perf_cond[perf] = (*phase_condition_)[well_cells[perf]];
}
const PhaseUsage& pu = fluid_->phaseUsage();
DataBlock b(nperf, pu.num_phases);
if (pu.phase_used[BlackoilPhases::Aqua]) {
const Vector bw = fluid_->bWat(avg_press_ad, perf_temp, well_cells).value();
b.col(pu.phase_pos[BlackoilPhases::Aqua]) = bw;
}
assert((*active_)[Oil]);
const Vector perf_so = subset(state.saturation[pu.phase_pos[Oil]].value(), well_cells);
if (pu.phase_used[BlackoilPhases::Liquid]) {
const ADB perf_rs = (state.rs.size() > 0) ? subset(state.rs, well_cells) : ADB::null();
const Vector bo = fluid_->bOil(avg_press_ad, perf_temp, perf_rs, perf_cond, well_cells).value();
b.col(pu.phase_pos[BlackoilPhases::Liquid]) = bo;
}
if (pu.phase_used[BlackoilPhases::Vapour]) {
const ADB perf_rv = (state.rv.size() > 0) ? subset(state.rv, well_cells) : ADB::null();
const Vector bg = fluid_->bGas(avg_press_ad, perf_temp, perf_rv, perf_cond, well_cells).value();
b.col(pu.phase_pos[BlackoilPhases::Vapour]) = bg;
}
if (pu.phase_used[BlackoilPhases::Liquid] && pu.phase_used[BlackoilPhases::Vapour]) {
const Vector rssat = fluid_->rsSat(ADB::constant(avg_press), ADB::constant(perf_so), well_cells).value();
rsmax_perf.assign(rssat.data(), rssat.data() + nperf);
const Vector rvsat = fluid_->rvSat(ADB::constant(avg_press), ADB::constant(perf_so), well_cells).value();
rvmax_perf.assign(rvsat.data(), rvsat.data() + nperf);
}
// b is row major, so can just copy data.
b_perf.assign(b.data(), b.data() + nperf * pu.num_phases);
// Surface density.
// The compute density segment wants the surface densities as
// an np * number of wells cells array
Vector rho = superset(fluid_->surfaceDensity(0 , well_cells), Span(nperf, pu.num_phases, 0), nperf*pu.num_phases);
for (int phase = 1; phase < pu.num_phases; ++phase) {
rho += superset(fluid_->surfaceDensity(phase , well_cells), Span(nperf, pu.num_phases, phase), nperf*pu.num_phases);
}
surf_dens_perf.assign(rho.data(), rho.data() + nperf * pu.num_phases);
}
template <class WellState>
void
StandardWells::
computeWellConnectionDensitesPressures(const WellState& xw,
const std::vector<double>& b_perf,
const std::vector<double>& rsmax_perf,
const std::vector<double>& rvmax_perf,
const std::vector<double>& surf_dens_perf,
const std::vector<double>& depth_perf,
const double grav)
{
// Compute densities
std::vector<double> cd =
WellDensitySegmented::computeConnectionDensities(
wells(), fluid_->phaseUsage(), xw.perfPhaseRates(),
b_perf, rsmax_perf, rvmax_perf, surf_dens_perf);
const int nperf = wells().well_connpos[wells().number_of_wells];
// Compute pressure deltas
std::vector<double> cdp =
WellDensitySegmented::computeConnectionPressureDelta(
wells(), depth_perf, cd, grav);
// Store the results
well_perforation_densities_ = Eigen::Map<const Vector>(cd.data(), nperf);
well_perforation_pressure_diffs_ = Eigen::Map<const Vector>(cdp.data(), nperf);
}
template <class SolutionState, class WellState>
void
StandardWells::
computeWellConnectionPressures(const SolutionState& state,
const WellState& xw)
{
if( ! localWellsActive() ) return ;
// 1. Compute properties required by computeConnectionPressureDelta().
// Note that some of the complexity of this part is due to the function
// taking std::vector<double> arguments, and not Eigen objects.
std::vector<double> b_perf;
std::vector<double> rsmax_perf;
std::vector<double> rvmax_perf;
std::vector<double> surf_dens_perf;
computePropertiesForWellConnectionPressures(state, xw, b_perf, rsmax_perf, rvmax_perf, surf_dens_perf);
const Vector& pdepth = perf_cell_depth_;
const int nperf = wells().well_connpos[wells().number_of_wells];
const std::vector<double> depth_perf(pdepth.data(), pdepth.data() + nperf);
computeWellConnectionDensitesPressures(xw, b_perf, rsmax_perf, rvmax_perf, surf_dens_perf, depth_perf, gravity_);
}
template <class ReservoirResidualQuant, class SolutionState>
void
StandardWells::
extractWellPerfProperties(const SolutionState& /* state */,
const std::vector<ReservoirResidualQuant>& rq,
std::vector<ADB>& mob_perfcells,
std::vector<ADB>& b_perfcells) const
{
// If we have wells, extract the mobilities and b-factors for
// the well-perforated cells.
if ( !localWellsActive() ) {
mob_perfcells.clear();
b_perfcells.clear();
return;
} else {
const std::vector<int>& well_cells = wellOps().well_cells;
const int num_phases = wells().number_of_phases;
mob_perfcells.resize(num_phases, ADB::null());
b_perfcells.resize(num_phases, ADB::null());
for (int phase = 0; phase < num_phases; ++phase) {
mob_perfcells[phase] = subset(rq[phase].mob, well_cells);
b_perfcells[phase] = subset(rq[phase].b, well_cells);
}
}
}
template <class SolutionState>
void
StandardWells::
computeWellFlux(const SolutionState& state,
const std::vector<ADB>& mob_perfcells,
const std::vector<ADB>& b_perfcells,
Vector& aliveWells,
std::vector<ADB>& cq_s) const
{
if( ! localWellsActive() ) return ;
const int np = wells().number_of_phases;
const int nw = wells().number_of_wells;
const int nperf = wells().well_connpos[nw];
Vector Tw = Eigen::Map<const Vector>(wells().WI, nperf);
const std::vector<int>& well_cells = wellOps().well_cells;
// pressure diffs computed already (once per step, not changing per iteration)
const Vector& cdp = wellPerforationPressureDiffs();
// Extract needed quantities for the perforation cells
const ADB& p_perfcells = subset(state.pressure, well_cells);
// Perforation pressure
const ADB perfpressure = (wellOps().w2p * state.bhp) + cdp;
// Pressure drawdown (also used to determine direction of flow)
const ADB drawdown = p_perfcells - perfpressure;
// Compute vectors with zero and ones that
// selects the wanted quantities.
// selects injection perforations
Vector selectInjectingPerforations = Vector::Zero(nperf);
// selects producing perforations
Vector selectProducingPerforations = Vector::Zero(nperf);
for (int c = 0; c < nperf; ++c){
if (drawdown.value()[c] < 0)
selectInjectingPerforations[c] = 1;
else
selectProducingPerforations[c] = 1;
}
// Handle cross flow
const Vector numInjectingPerforations = (wellOps().p2w * ADB::constant(selectInjectingPerforations)).value();
const Vector numProducingPerforations = (wellOps().p2w * ADB::constant(selectProducingPerforations)).value();
for (int w = 0; w < nw; ++w) {
if (!wells().allow_cf[w]) {
for (int perf = wells().well_connpos[w] ; perf < wells().well_connpos[w+1]; ++perf) {
// Crossflow is not allowed; reverse flow is prevented.
// At least one of the perforation must be open in order to have a meeningful
// equation to solve. For the special case where all perforations have reverse flow,
// and the target rate is non-zero all of the perforations are keept open.
if (wells().type[w] == INJECTOR && numInjectingPerforations[w] > 0) {
selectProducingPerforations[perf] = 0.0;
} else if (wells().type[w] == PRODUCER && numProducingPerforations[w] > 0 ){
selectInjectingPerforations[perf] = 0.0;
}
}
}
}
// HANDLE FLOW INTO WELLBORE
// compute phase volumetric rates at standard conditions
std::vector<ADB> cq_p(np, ADB::null());
std::vector<ADB> cq_ps(np, ADB::null());
for (int phase = 0; phase < np; ++phase) {
cq_p[phase] = -(selectProducingPerforations * Tw) * (mob_perfcells[phase] * drawdown);
cq_ps[phase] = b_perfcells[phase] * cq_p[phase];
}
const Opm::PhaseUsage& pu = fluid_->phaseUsage();
if ((*active_)[Oil] && (*active_)[Gas]) {
const int oilpos = pu.phase_pos[Oil];
const int gaspos = pu.phase_pos[Gas];
const ADB cq_psOil = cq_ps[oilpos];
const ADB cq_psGas = cq_ps[gaspos];
const ADB& rv_perfcells = subset(state.rv, well_cells);
const ADB& rs_perfcells = subset(state.rs, well_cells);
cq_ps[gaspos] += rs_perfcells * cq_psOil;
cq_ps[oilpos] += rv_perfcells * cq_psGas;
}
// HANDLE FLOW OUT FROM WELLBORE
// Using total mobilities
ADB total_mob = mob_perfcells[0];
for (int phase = 1; phase < np; ++phase) {
total_mob += mob_perfcells[phase];
}
// injection perforations total volume rates
const ADB cqt_i = -(selectInjectingPerforations * Tw) * (total_mob * drawdown);
// Store well perforation total fluxes (reservor volumes) if requested.
if (store_well_perforation_fluxes_) {
// Ugly const-cast, but unappealing alternatives.
Vector& wf = const_cast<Vector&>(well_perforation_fluxes_);
wf = cqt_i.value();
for (int phase = 0; phase < np; ++phase) {
wf += cq_p[phase].value();
}
}
// compute wellbore mixture for injecting perforations
// The wellbore mixture depends on the inflow from the reservoar
// and the well injection rates.
// compute avg. and total wellbore phase volumetric rates at standard conds
const DataBlock compi = Eigen::Map<const DataBlock>(wells().comp_frac, nw, np);
std::vector<ADB> wbq(np, ADB::null());
ADB wbqt = ADB::constant(Vector::Zero(nw));
for (int phase = 0; phase < np; ++phase) {
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];
const int perf = wells().well_connpos[w]; //first perforation.
if (well_type == INJECTOR) {
double dp = wellhelpers::computeHydrostaticCorrection(
wells(), w, vfp_properties_->getInj()->getTable(table_id)->getDatumDepth(),
wellPerforationDensities()[perf], 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()[perf], 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
{
wellhelpers::WellSwitchingLogger logger;
if( !localWellsActive() ) return ;
// 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);
// There should be at least one control
assert(nwc != 0);
bool constraint_violated = false;
int number_iterations = 0;
const int max_iterations = 2 * nwc; // maximum allowed iterations
do {
updateWellStateWithTarget(wc, current, w, xw);
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.
logger.wellSwitched(wells().name[w],
well_controls_iget_type(wc, current),
well_controls_iget_type(wc, ctrl_index));
xw.currentControls()[w] = ctrl_index;
current = xw.currentControls()[w];
constraint_violated = true;
} else {
constraint_violated = false;
}
++number_iterations;
if (number_iterations > max_iterations) {
OPM_THROW(Opm::NumericalIssue, "Could not find proper control within " << number_iterations << " iterations!");
break;
}
} while (constraint_violated);
if (wellCollection()->groupControlActive()) {
// get well node in the well collection
WellNode& well_node = well_collection_->findWellNode(std::string(wells().name[w]));
// update whehter the well is under group control or individual control
if (well_node.groupControlIndex() >= 0 && current == well_node.groupControlIndex()) {
// under group control
well_node.setIndividualControl(false);
} else {
// individual control
well_node.setIndividualControl(true);
}
}
}
}
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,
const WellState& well_state,
SolutionState& state0,
std::vector<double>& well_potentials) const
{
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];
const int perf = wells().well_connpos[w]; //first perforation
if (well_type == INJECTOR) {
double dp = wellhelpers::computeHydrostaticCorrection(
wells(), w, vfp_properties_->getInj()->getTable(vfp)->getDatumDepth(),
wellPerforationDensities()[perf], 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()[perf], 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> perf_potentials;
computeWellFlux(state0, mob_perfcells, b_perfcells, aliveWells, perf_potentials);
well_potentials.resize(nw * np, 0.0);
for (int p = 0; p < np; ++p) {
for (int w = 0; w < nw; ++w) {
for (int perf = wells().well_connpos[w]; perf < wells().well_connpos[w + 1]; ++perf) {
well_potentials[w * np + p] += perf_potentials[p].value()[perf];
}
}
}
}
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_;
}
template<class WellState>
void
StandardWells::
updateListEconLimited(const Schedule& schedule,
const int current_step,
const Wells* wells_struct,
const WellState& well_state,
DynamicListEconLimited& list_econ_limited) const
{
// wells_struct may be null pointer if there are no wells in process domain
const int nw = ( wells_struct ) ? wells_struct->number_of_wells : 0;
for (int w = 0; w < nw; ++w) {
// flag to check if the mim oil/gas rate limit is violated
bool rate_limit_violated = false;
const std::string& well_name = wells_struct->name[w];
const Well* well_ecl = schedule.getWell(well_name);
const WellEconProductionLimits& econ_production_limits = well_ecl->getEconProductionLimits(current_step);
// economic limits only apply for production wells.
if (wells_struct->type[w] != PRODUCER) {
continue;
}
// if no limit is effective here, then continue to the next well
if ( !econ_production_limits.onAnyEffectiveLimit() ) {
continue;
}
// for the moment, we only handle rate limits, not handling potential limits
// the potential limits should not be difficult to add
const WellEcon::QuantityLimitEnum& quantity_limit = econ_production_limits.quantityLimit();
if (quantity_limit == WellEcon::POTN) {
const std::string msg = std::string("POTN limit for well ") + well_name + std::string(" is not supported for the moment. \n")
+ std::string("All the limits will be evaluated based on RATE. ");
OpmLog::warning("NOT_SUPPORTING_POTN", msg);
}
const WellMapType& well_map = well_state.wellMap();
const typename WellMapType::const_iterator i_well = well_map.find(well_name);
assert(i_well != well_map.end()); // should always be found?
const WellMapEntryType& map_entry = i_well->second;
const int well_number = map_entry[0];
if (econ_production_limits.onAnyRateLimit()) {
rate_limit_violated = checkRateEconLimits(econ_production_limits, well_state, well_number);
}
if (rate_limit_violated) {
if (econ_production_limits.endRun()) {
const std::string warning_message = std::string("ending run after well closed due to economic limits is not supported yet \n")
+ std::string("the program will keep running after ") + well_name + std::string(" is closed");
OpmLog::warning("NOT_SUPPORTING_ENDRUN", warning_message);
}
if (econ_production_limits.validFollowonWell()) {
OpmLog::warning("NOT_SUPPORTING_FOLLOWONWELL", "opening following on well after well closed is not supported yet");
}
if (well_ecl->getAutomaticShutIn()) {
list_econ_limited.addShutWell(well_name);
const std::string msg = std::string("well ") + well_name + std::string(" will be shut in due to economic limit");
OpmLog::info(msg);
} else {
list_econ_limited.addStoppedWell(well_name);
const std::string msg = std::string("well ") + well_name + std::string(" will be stopped due to economic limit");
OpmLog::info(msg);
}
// the well is closed, not need to check other limits
continue;
}
// checking for ratio related limits, mostly all kinds of ratio.
bool ratio_limits_violated = false;
RatioCheckTuple ratio_check_return;
if (econ_production_limits.onAnyRatioLimit()) {
ratio_check_return = checkRatioEconLimits(econ_production_limits, well_state, map_entry);
ratio_limits_violated = std::get<0>(ratio_check_return);
}
if (ratio_limits_violated) {
const bool last_connection = std::get<1>(ratio_check_return);
const int worst_offending_connection = std::get<2>(ratio_check_return);
const int perf_start = map_entry[1];
assert((worst_offending_connection >= 0) && (worst_offending_connection < map_entry[2]));
const int cell_worst_offending_connection = wells_struct->well_cells[perf_start + worst_offending_connection];
list_econ_limited.addClosedConnectionsForWell(well_name, cell_worst_offending_connection);
const std::string msg = std::string("Connection ") + std::to_string(worst_offending_connection) + std::string(" for well ")
+ well_name + std::string(" will be closed due to economic limit");
OpmLog::info(msg);
if (last_connection) {
list_econ_limited.addShutWell(well_name);
const std::string msg2 = well_name + std::string(" will be shut due to the last connection closed");
OpmLog::info(msg2);
}
}
}
}
template <class WellState>
bool
StandardWells::
checkRateEconLimits(const WellEconProductionLimits& econ_production_limits,
const WellState& well_state,
const int well_number) const
{
const Opm::PhaseUsage& pu = fluid_->phaseUsage();
const int np = well_state.numPhases();
if (econ_production_limits.onMinOilRate()) {
assert((*active_)[Oil]);
const double oil_rate = well_state.wellRates()[well_number * np + pu.phase_pos[ Oil ] ];
const double min_oil_rate = econ_production_limits.minOilRate();
if (std::abs(oil_rate) < min_oil_rate) {
return true;
}
}
if (econ_production_limits.onMinGasRate() ) {
assert((*active_)[Gas]);
const double gas_rate = well_state.wellRates()[well_number * np + pu.phase_pos[ Gas ] ];
const double min_gas_rate = econ_production_limits.minGasRate();
if (std::abs(gas_rate) < min_gas_rate) {
return true;
}
}
if (econ_production_limits.onMinLiquidRate() ) {
assert((*active_)[Oil]);
assert((*active_)[Water]);
const double oil_rate = well_state.wellRates()[well_number * np + pu.phase_pos[ Oil ] ];
const double water_rate = well_state.wellRates()[well_number * np + pu.phase_pos[ Water ] ];
const double liquid_rate = oil_rate + water_rate;
const double min_liquid_rate = econ_production_limits.minLiquidRate();
if (std::abs(liquid_rate) < min_liquid_rate) {
return true;
}
}
if (econ_production_limits.onMinReservoirFluidRate()) {
OpmLog::warning("NOT_SUPPORTING_MIN_RESERVOIR_FLUID_RATE", "Minimum reservoir fluid production rate limit is not supported yet");
}
return false;
}
template <class WellState>
StandardWells::RatioCheckTuple
StandardWells::
checkRatioEconLimits(const WellEconProductionLimits& econ_production_limits,
const WellState& well_state,
const WellMapEntryType& map_entry) const
{
// TODO: not sure how to define the worst-offending connection when more than one
// ratio related limit is violated.
// The defintion used here is that we define the violation extent based on the
// ratio between the value and the corresponding limit.
// For each violated limit, we decide the worst-offending connection separately.
// Among the worst-offending connections, we use the one has the biggest violation
// extent.
bool any_limit_violated = false;
bool last_connection = false;
int worst_offending_connection = INVALIDCONNECTION;
double violation_extent = -1.0;
if (econ_production_limits.onMaxWaterCut()) {
const RatioCheckTuple water_cut_return = checkMaxWaterCutLimit(econ_production_limits, well_state, map_entry);
bool water_cut_violated = std::get<0>(water_cut_return);
if (water_cut_violated) {
any_limit_violated = true;
const double violation_extent_water_cut = std::get<3>(water_cut_return);
if (violation_extent_water_cut > violation_extent) {
violation_extent = violation_extent_water_cut;
worst_offending_connection = std::get<2>(water_cut_return);
last_connection = std::get<1>(water_cut_return);
}
}
}
if (econ_production_limits.onMaxGasOilRatio()) {
OpmLog::warning("NOT_SUPPORTING_MAX_GOR", "the support for max Gas-Oil ratio is not implemented yet!");
}
if (econ_production_limits.onMaxWaterGasRatio()) {
OpmLog::warning("NOT_SUPPORTING_MAX_WGR", "the support for max Water-Gas ratio is not implemented yet!");
}
if (econ_production_limits.onMaxGasLiquidRatio()) {
OpmLog::warning("NOT_SUPPORTING_MAX_GLR", "the support for max Gas-Liquid ratio is not implemented yet!");
}
if (any_limit_violated) {
assert(worst_offending_connection >=0);
assert(violation_extent > 1.);
}
return std::make_tuple(any_limit_violated, last_connection, worst_offending_connection, violation_extent);
}
template <class WellState>
StandardWells::RatioCheckTuple
StandardWells::
checkMaxWaterCutLimit(const WellEconProductionLimits& econ_production_limits,
const WellState& well_state,
const WellMapEntryType& map_entry) const
{
bool water_cut_limit_violated = false;
int worst_offending_connection = INVALIDCONNECTION;
bool last_connection = false;
double violation_extent = -1.0;
const int np = well_state.numPhases();
const Opm::PhaseUsage& pu = fluid_->phaseUsage();
const int well_number = map_entry[0];
assert((*active_)[Oil]);
assert((*active_)[Water]);
const double oil_rate = well_state.wellRates()[well_number * np + pu.phase_pos[ Oil ] ];
const double water_rate = well_state.wellRates()[well_number * np + pu.phase_pos[ Water ] ];
const double liquid_rate = oil_rate + water_rate;
double water_cut;
if (std::abs(liquid_rate) != 0.) {
water_cut = water_rate / liquid_rate;
} else {
water_cut = 0.0;
}
const double max_water_cut_limit = econ_production_limits.maxWaterCut();
if (water_cut > max_water_cut_limit) {
water_cut_limit_violated = true;
}
if (water_cut_limit_violated) {
// need to handle the worst_offending_connection
const int perf_start = map_entry[1];
const int perf_number = map_entry[2];
std::vector<double> water_cut_perf(perf_number);
for (int perf = 0; perf < perf_number; ++perf) {
const int i_perf = perf_start + perf;
const double oil_perf_rate = well_state.perfPhaseRates()[i_perf * np + pu.phase_pos[ Oil ] ];
const double water_perf_rate = well_state.perfPhaseRates()[i_perf * np + pu.phase_pos[ Water ] ];
const double liquid_perf_rate = oil_perf_rate + water_perf_rate;
if (std::abs(liquid_perf_rate) != 0.) {
water_cut_perf[perf] = water_perf_rate / liquid_perf_rate;
} else {
water_cut_perf[perf] = 0.;
}
}
last_connection = (perf_number == 1);
if (last_connection) {
worst_offending_connection = 0;
violation_extent = water_cut_perf[0] / max_water_cut_limit;
return std::make_tuple(water_cut_limit_violated, last_connection, worst_offending_connection, violation_extent);
}
double max_water_cut_perf = 0.;
for (int perf = 0; perf < perf_number; ++perf) {
if (water_cut_perf[perf] > max_water_cut_perf) {
worst_offending_connection = perf;
max_water_cut_perf = water_cut_perf[perf];
}
}
assert(max_water_cut_perf != 0.);
assert((worst_offending_connection >= 0) && (worst_offending_connection < perf_number));
violation_extent = max_water_cut_perf / max_water_cut_limit;
}
return std::make_tuple(water_cut_limit_violated, last_connection, worst_offending_connection, violation_extent);
}
WellCollection* StandardWells::wellCollection() const
{
return well_collection_;
}
void StandardWells::calculateEfficiencyFactors()
{
if ( !localWellsActive() ) {
return;
}
// get efficiency factor for each well first
const int nw = wells_->number_of_wells;
Vector well_efficiency_factors = Vector::Ones(nw);
for (int w = 0; w < nw; ++w) {
const std::string well_name = wells_->name[w];
const WellNode& well_node = well_collection_->findWellNode(well_name);
well_efficiency_factors(w) = well_node.getAccumulativeEfficiencyFactor();
}
// map them to the perforation.
well_perforation_efficiency_factors_ = wellOps().w2p * well_efficiency_factors.matrix();
}
const StandardWells::Vector&
StandardWells::wellPerfEfficiencyFactors() const
{
return well_perforation_efficiency_factors_;
}
int StandardWells::currentStep() const
{
return current_step_;
}
template <class WellState>
void
StandardWells::
updateWellStateWithTarget(const WellControls* wc,
const int current,
const int well_index,
WellState& xw) const
{
const int np = wells().number_of_phases;
// 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()[well_index] = 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()[well_index*np + pu.phase_pos[ Water ] ];
}
if ((*active_)[ Oil ]) {
liquid = xw.wellRates()[well_index*np + pu.phase_pos[ Oil ] ];
}
if ((*active_)[ Gas ]) {
vapour = xw.wellRates()[well_index*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[well_index];
// pick the density in the top layer
const int perf = wells().well_connpos[well_index];
const double rho = well_perforation_densities_[perf];
if (well_type == INJECTOR) {
double dp = wellhelpers::computeHydrostaticCorrection(
wells(), well_index, vfp_properties_->getInj()->getTable(vfp)->getDatumDepth(),
rho, gravity_);
xw.bhp()[well_index] = vfp_properties_->getInj()->bhp(vfp, aqua, liquid, vapour, thp) - dp;
}
else if (well_type == PRODUCER) {
double dp = wellhelpers::computeHydrostaticCorrection(
wells(), well_index, vfp_properties_->getProd()->getTable(vfp)->getDatumDepth(),
rho, gravity_);
xw.bhp()[well_index] = 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[well_index];
if (well_type == INJECTOR) {
for (int phase = 0; phase < np; ++phase) {
const double& compi = wells().comp_frac[np * well_index + phase];
if (compi > 0.0) {
xw.wellRates()[np * well_index + 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 * well_index + phase] = target * distr[phase];
}
}
} else {
OPM_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well");
}
break;
}
}
} // namespace Opm
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