mirror of
https://github.com/OPM/opm-simulators.git
synced 2024-12-28 18:21:00 -06:00
734 lines
29 KiB
C++
734 lines
29 KiB
C++
/*
|
|
Copyright 2017 SINTEF Digital, Mathematics and Cybernetics.
|
|
Copyright 2017 Statoil ASA.
|
|
Copyright 2016 - 2017 IRIS AS.
|
|
|
|
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 <config.h>
|
|
#include <opm/simulators/wells/StandardWellPrimaryVariables.hpp>
|
|
|
|
#include <opm/common/Exceptions.hpp>
|
|
|
|
#include <dune/common/dynvector.hh>
|
|
#include <dune/istl/bvector.hh>
|
|
|
|
#include <opm/material/densead/Evaluation.hpp>
|
|
#include <opm/material/fluidsystems/BlackOilFluidSystem.hpp>
|
|
|
|
#include <opm/models/blackoil/blackoilindices.hh>
|
|
#include <opm/models/blackoil/blackoilonephaseindices.hh>
|
|
#include <opm/models/blackoil/blackoiltwophaseindices.hh>
|
|
|
|
#include <opm/simulators/utils/DeferredLoggingErrorHelpers.hpp>
|
|
|
|
#include <opm/simulators/wells/WellInterfaceIndices.hpp>
|
|
#include <opm/simulators/wells/WellState.hpp>
|
|
|
|
#include <algorithm>
|
|
#include <cassert>
|
|
|
|
namespace {
|
|
|
|
//! \brief Relaxation factor considering only one fraction value.
|
|
template<class Scalar>
|
|
Scalar relaxationFactorFraction(const Scalar old_value,
|
|
const Scalar dx)
|
|
{
|
|
assert(old_value >= 0. && old_value <= 1.0);
|
|
|
|
Scalar relaxation_factor = 1.;
|
|
|
|
// updated values without relaxation factor
|
|
const Scalar possible_updated_value = old_value - dx;
|
|
|
|
// 0.95 is an experimental value remains to be optimized
|
|
if (possible_updated_value < 0.0) {
|
|
relaxation_factor = std::abs(old_value / dx) * 0.95;
|
|
} else if (possible_updated_value > 1.0) {
|
|
relaxation_factor = std::abs((1. - old_value) / dx) * 0.95;
|
|
}
|
|
// if possible_updated_value is between 0. and 1.0, then relaxation_factor
|
|
// remains to be one
|
|
|
|
assert(relaxation_factor >= 0. && relaxation_factor <= 1.);
|
|
|
|
return relaxation_factor;
|
|
}
|
|
|
|
//! \brief Calculate a relaxation factor to avoid overshoot of total rates.
|
|
template<class Scalar>
|
|
Scalar relaxationFactorRate(const Scalar old_value,
|
|
const Scalar newton_update)
|
|
{
|
|
Scalar relaxation_factor = 1.0;
|
|
|
|
// For injector, we only check the total rates to avoid sign change of rates
|
|
const Scalar original_total_rate = old_value;
|
|
const Scalar possible_update_total_rate = old_value - newton_update;
|
|
|
|
// 0.8 here is a experimental value, which remains to be optimized
|
|
// if the original rate is zero or possible_update_total_rate is zero, relaxation_factor will
|
|
// always be 1.0, more thoughts might be needed.
|
|
if (original_total_rate * possible_update_total_rate < 0.) { // sign changed
|
|
relaxation_factor = std::abs(original_total_rate / newton_update) * 0.8;
|
|
}
|
|
|
|
assert(relaxation_factor >= 0.0 && relaxation_factor <= 1.0);
|
|
|
|
return relaxation_factor;
|
|
}
|
|
|
|
}
|
|
|
|
namespace Opm {
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
init()
|
|
{
|
|
for (int eqIdx = 0; eqIdx < numWellEq_; ++eqIdx) {
|
|
evaluation_[eqIdx] =
|
|
EvalWell::createVariable(numWellEq_ + Indices::numEq,
|
|
value_[eqIdx],
|
|
Indices::numEq + eqIdx);
|
|
|
|
}
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
resize(const int numWellEq)
|
|
{
|
|
value_.resize(numWellEq, 0.0);
|
|
evaluation_.resize(numWellEq, EvalWell{numWellEq + Indices::numEq, 0.0});
|
|
numWellEq_ = numWellEq;
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
update(const WellState& well_state, DeferredLogger& deferred_logger)
|
|
{
|
|
static constexpr int Water = BlackoilPhases::Aqua;
|
|
static constexpr int Oil = BlackoilPhases::Liquid;
|
|
static constexpr int Gas = BlackoilPhases::Vapour;
|
|
|
|
const int well_index = well_.indexOfWell();
|
|
const int np = well_.numPhases();
|
|
const auto& pu = well_.phaseUsage();
|
|
const auto& ws = well_state.well(well_index);
|
|
// the weighted total well rate
|
|
double total_well_rate = 0.0;
|
|
for (int p = 0; p < np; ++p) {
|
|
total_well_rate += well_.scalingFactor(p) * ws.surface_rates[p];
|
|
}
|
|
|
|
// Not: for the moment, the first primary variable for the injectors is not G_total. The injection rate
|
|
// under surface condition is used here
|
|
if (well_.isInjector()) {
|
|
switch (well_.wellEcl().injectorType()) {
|
|
case InjectorType::WATER:
|
|
value_[WQTotal] = ws.surface_rates[pu.phase_pos[Water]];
|
|
break;
|
|
case InjectorType::GAS:
|
|
value_[WQTotal] = ws.surface_rates[pu.phase_pos[Gas]];
|
|
break;
|
|
case InjectorType::OIL:
|
|
value_[WQTotal] = ws.surface_rates[pu.phase_pos[Oil]];
|
|
break;
|
|
case InjectorType::MULTI:
|
|
// Not supported.
|
|
deferred_logger.warning("MULTI_PHASE_INJECTOR_NOT_SUPPORTED",
|
|
"Multi phase injectors are not supported, requested for well " + well_.name());
|
|
break;
|
|
}
|
|
} else {
|
|
value_[WQTotal] = total_well_rate;
|
|
}
|
|
|
|
if (std::abs(total_well_rate) > 0.) {
|
|
if constexpr (has_wfrac_variable) {
|
|
value_[WFrac] = well_.scalingFactor(pu.phase_pos[Water]) * ws.surface_rates[pu.phase_pos[Water]] / total_well_rate;
|
|
}
|
|
if constexpr (has_gfrac_variable) {
|
|
value_[GFrac] = well_.scalingFactor(pu.phase_pos[Gas]) *
|
|
(ws.surface_rates[pu.phase_pos[Gas]] -
|
|
(Indices::enableSolvent ? ws.sum_solvent_rates() : 0.0) ) / total_well_rate ;
|
|
}
|
|
if constexpr (Indices::enableSolvent) {
|
|
value_[SFrac] = well_.scalingFactor(pu.phase_pos[Gas]) * ws.sum_solvent_rates() / total_well_rate ;
|
|
}
|
|
} else { // total_well_rate == 0
|
|
if (well_.isInjector()) {
|
|
// only single phase injection handled
|
|
if constexpr (has_wfrac_variable) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
auto phase = well_.wellEcl().getInjectionProperties().injectorType;
|
|
if (phase == InjectorType::WATER) {
|
|
value_[WFrac] = 1.0;
|
|
} else {
|
|
value_[WFrac] = 0.0;
|
|
}
|
|
}
|
|
}
|
|
if constexpr (has_gfrac_variable) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
auto phase = well_.wellEcl().getInjectionProperties().injectorType;
|
|
if (phase == InjectorType::GAS) {
|
|
value_[GFrac] = (1.0 - well_.rsRvInj());
|
|
if constexpr (Indices::enableSolvent) {
|
|
value_[GFrac] = 1.0 - well_.rsRvInj() - well_.wsolvent();
|
|
value_[SFrac] = well_.wsolvent();
|
|
}
|
|
} else {
|
|
value_[GFrac] = 0.0;
|
|
}
|
|
}
|
|
}
|
|
|
|
// TODO: it is possible to leave injector as a oil well,
|
|
// when F_w and F_g both equals to zero, not sure under what kind of circumstance
|
|
// this will happen.
|
|
} else if (well_.isProducer()) { // producers
|
|
// TODO: the following are not addressed for the solvent case yet
|
|
if constexpr (has_wfrac_variable) {
|
|
value_[WFrac] = 1.0 / np;
|
|
}
|
|
|
|
if constexpr (has_gfrac_variable) {
|
|
value_[GFrac] = 1.0 / np;
|
|
}
|
|
} else {
|
|
OPM_DEFLOG_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well", deferred_logger);
|
|
}
|
|
}
|
|
|
|
// BHP
|
|
value_[Bhp] = ws.bhp;
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
updatePolyMW(const WellState& well_state)
|
|
{
|
|
if (well_.isInjector()) {
|
|
const auto& ws = well_state.well(well_.indexOfWell());
|
|
const auto& perf_data = ws.perf_data;
|
|
const auto& water_velocity = perf_data.water_velocity;
|
|
const auto& skin_pressure = perf_data.skin_pressure;
|
|
for (int perf = 0; perf < well_.numPerfs(); ++perf) {
|
|
value_[Bhp + 1 + perf] = water_velocity[perf];
|
|
value_[Bhp + 1 + well_.numPerfs() + perf] = skin_pressure[perf];
|
|
}
|
|
}
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
updateNewton(const BVectorWell& dwells,
|
|
[[maybe_unused]] const double dFLimit,
|
|
const double dBHPLimit)
|
|
{
|
|
const double relaxation_factor_rate = relaxationFactorRate(value_[WQTotal],
|
|
dwells[0][WQTotal]);
|
|
|
|
// for injectors, very typical one of the fractions will be one, and it is easy to get zero value
|
|
// fractions. not sure what is the best way to handle it yet, so we just use 1.0 here
|
|
[[maybe_unused]] const double relaxation_factor_fractions =
|
|
well_.isProducer() ? this->relaxationFactorFractionsProducer(dwells) : 1.0;
|
|
|
|
// update the second and third well variable (The flux fractions)
|
|
|
|
if constexpr (has_wfrac_variable) {
|
|
const int sign2 = dwells[0][WFrac] > 0 ? 1: -1;
|
|
const double dx2_limited = sign2 * std::min(std::abs(dwells[0][WFrac] * relaxation_factor_fractions), dFLimit);
|
|
value_[WFrac] = value_[WFrac] - dx2_limited;
|
|
}
|
|
|
|
if constexpr (has_gfrac_variable) {
|
|
const int sign3 = dwells[0][GFrac] > 0 ? 1: -1;
|
|
const double dx3_limited = sign3 * std::min(std::abs(dwells[0][GFrac] * relaxation_factor_fractions), dFLimit);
|
|
value_[GFrac] = value_[GFrac] - dx3_limited;
|
|
}
|
|
|
|
if constexpr (Indices::enableSolvent) {
|
|
const int sign4 = dwells[0][SFrac] > 0 ? 1: -1;
|
|
const double dx4_limited = sign4 * std::min(std::abs(dwells[0][SFrac]) * relaxation_factor_fractions, dFLimit);
|
|
value_[SFrac] = value_[SFrac] - dx4_limited;
|
|
}
|
|
|
|
this->processFractions();
|
|
|
|
// updating the total rates Q_t
|
|
value_[WQTotal] = value_[WQTotal] - dwells[0][WQTotal] * relaxation_factor_rate;
|
|
|
|
// updating the bottom hole pressure
|
|
const int sign1 = dwells[0][Bhp] > 0 ? 1: -1;
|
|
const double dx1_limited = sign1 * std::min(std::abs(dwells[0][Bhp]),
|
|
std::abs(value_[Bhp]) * dBHPLimit);
|
|
// 1e5 to make sure bhp will not be below 1bar
|
|
value_[Bhp] = std::max(value_[Bhp] - dx1_limited, 1e5);
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
updateNewtonPolyMW(const BVectorWell& dwells)
|
|
{
|
|
if (well_.isInjector()) {
|
|
for (int perf = 0; perf < well_.numPerfs(); ++perf) {
|
|
const int wat_vel_index = Bhp + 1 + perf;
|
|
const int pskin_index = Bhp + 1 + well_.numPerfs() + perf;
|
|
|
|
const double relaxation_factor = 0.9;
|
|
const double dx_wat_vel = dwells[0][wat_vel_index];
|
|
value_[wat_vel_index] -= relaxation_factor * dx_wat_vel;
|
|
|
|
const double dx_pskin = dwells[0][pskin_index];
|
|
value_[pskin_index] -= relaxation_factor * dx_pskin;
|
|
}
|
|
}
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
copyToWellState(WellState& well_state,
|
|
DeferredLogger& deferred_logger) const
|
|
{
|
|
static constexpr int Water = BlackoilPhases::Aqua;
|
|
static constexpr int Oil = BlackoilPhases::Liquid;
|
|
static constexpr int Gas = BlackoilPhases::Vapour;
|
|
|
|
const PhaseUsage& pu = well_.phaseUsage();
|
|
std::vector<double> F(well_.numPhases(), 0.0);
|
|
[[maybe_unused]] double F_solvent = 0.0;
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
const int oil_pos = pu.phase_pos[Oil];
|
|
F[oil_pos] = 1.0;
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
const int water_pos = pu.phase_pos[Water];
|
|
F[water_pos] = value_[WFrac];
|
|
F[oil_pos] -= F[water_pos];
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
const int gas_pos = pu.phase_pos[Gas];
|
|
F[gas_pos] = value_[GFrac];
|
|
F[oil_pos] -= F[gas_pos];
|
|
}
|
|
|
|
if constexpr (Indices::enableSolvent) {
|
|
F_solvent = value_[SFrac];
|
|
F[oil_pos] -= F_solvent;
|
|
}
|
|
}
|
|
else if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
const int water_pos = pu.phase_pos[Water];
|
|
F[water_pos] = 1.0;
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
const int gas_pos = pu.phase_pos[Gas];
|
|
F[gas_pos] = value_[GFrac];
|
|
F[water_pos] -= F[gas_pos];
|
|
}
|
|
}
|
|
else if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
const int gas_pos = pu.phase_pos[Gas];
|
|
F[gas_pos] = 1.0;
|
|
}
|
|
|
|
// convert the fractions to be Q_p / G_total to calculate the phase rates
|
|
for (int p = 0; p < well_.numPhases(); ++p) {
|
|
const double scal = well_.scalingFactor(p);
|
|
// for injection wells, there should only one non-zero scaling factor
|
|
if (scal > 0) {
|
|
F[p] /= scal ;
|
|
} else {
|
|
// this should only happens to injection wells
|
|
F[p] = 0.;
|
|
}
|
|
}
|
|
|
|
// F_solvent is added to F_gas. This means that well_rate[Gas] also contains solvent.
|
|
// More testing is needed to make sure this is correct for well groups and THP.
|
|
if constexpr (Indices::enableSolvent) {
|
|
F_solvent /= well_.scalingFactor(Indices::contiSolventEqIdx);
|
|
F[pu.phase_pos[Gas]] += F_solvent;
|
|
}
|
|
|
|
auto& ws = well_state.well(well_.indexOfWell());
|
|
ws.bhp = value_[Bhp];
|
|
|
|
// calculate the phase rates based on the primary variables
|
|
// for producers, this is not a problem, while not sure for injectors here
|
|
if (well_.isProducer()) {
|
|
const double g_total = value_[WQTotal];
|
|
for (int p = 0; p < well_.numPhases(); ++p) {
|
|
ws.surface_rates[p] = g_total * F[p];
|
|
}
|
|
} else { // injectors
|
|
for (int p = 0; p < well_.numPhases(); ++p) {
|
|
ws.surface_rates[p] = 0.0;
|
|
}
|
|
switch (well_.wellEcl().injectorType()) {
|
|
case InjectorType::WATER:
|
|
ws.surface_rates[pu.phase_pos[Water]] = value_[WQTotal];
|
|
break;
|
|
case InjectorType::GAS:
|
|
ws.surface_rates[pu.phase_pos[Gas]] = value_[WQTotal];
|
|
break;
|
|
case InjectorType::OIL:
|
|
ws.surface_rates[pu.phase_pos[Oil]] = value_[WQTotal];
|
|
break;
|
|
case InjectorType::MULTI:
|
|
// Not supported.
|
|
deferred_logger.warning("MULTI_PHASE_INJECTOR_NOT_SUPPORTED",
|
|
"Multi phase injectors are not supported, requested for well " + well_.name());
|
|
break;
|
|
}
|
|
}
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
copyToWellStatePolyMW(WellState& well_state) const
|
|
{
|
|
if (well_.isInjector()) {
|
|
auto& ws = well_state.well(well_.indexOfWell());
|
|
auto& perf_data = ws.perf_data;
|
|
auto& perf_water_velocity = perf_data.water_velocity;
|
|
auto& perf_skin_pressure = perf_data.skin_pressure;
|
|
for (int perf = 0; perf < well_.numPerfs(); ++perf) {
|
|
perf_water_velocity[perf] = value_[Bhp + 1 + perf];
|
|
perf_skin_pressure[perf] = value_[Bhp + 1 + well_.numPerfs() + perf];
|
|
}
|
|
}
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
typename StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::EvalWell
|
|
StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
volumeFraction(const unsigned compIdx) const
|
|
{
|
|
if (FluidSystem::numActivePhases() == 1) {
|
|
return EvalWell(numWellEq_ + Indices::numEq, 1.0);
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
if (has_wfrac_variable && compIdx == Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx)) {
|
|
return evaluation_[WFrac];
|
|
}
|
|
|
|
if (has_gfrac_variable && compIdx == Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx)) {
|
|
return evaluation_[GFrac];
|
|
}
|
|
|
|
if (Indices::enableSolvent && compIdx == (unsigned)Indices::contiSolventEqIdx) {
|
|
return evaluation_[SFrac];
|
|
}
|
|
}
|
|
else if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
if (has_gfrac_variable && compIdx == Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx)) {
|
|
return evaluation_[GFrac];
|
|
}
|
|
}
|
|
|
|
// Oil or WATER fraction
|
|
EvalWell well_fraction(numWellEq_ + Indices::numEq, 1.0);
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
well_fraction -= evaluation_[WFrac];
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
well_fraction -= evaluation_[GFrac];
|
|
}
|
|
|
|
if constexpr (Indices::enableSolvent) {
|
|
well_fraction -= evaluation_[SFrac];
|
|
}
|
|
}
|
|
else if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx) &&
|
|
FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
well_fraction -= evaluation_[GFrac];
|
|
}
|
|
|
|
return well_fraction;
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
typename StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::EvalWell
|
|
StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
volumeFractionScaled(const int compIdx) const
|
|
{
|
|
const int legacyCompIdx = well_.ebosCompIdxToFlowCompIdx(compIdx);
|
|
const double scal = well_.scalingFactor(legacyCompIdx);
|
|
if (scal > 0)
|
|
return this->volumeFraction(compIdx) / scal;
|
|
|
|
// the scaling factor may be zero for RESV controlled wells.
|
|
return this->volumeFraction(compIdx);
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
typename StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::EvalWell
|
|
StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
surfaceVolumeFraction(const int compIdx) const
|
|
{
|
|
EvalWell sum_volume_fraction_scaled(numWellEq_ + Indices::numEq, 0.);
|
|
for (int idx = 0; idx < well_.numComponents(); ++idx) {
|
|
sum_volume_fraction_scaled += this->volumeFractionScaled(idx);
|
|
}
|
|
|
|
assert(sum_volume_fraction_scaled.value() != 0.);
|
|
|
|
return this->volumeFractionScaled(compIdx) / sum_volume_fraction_scaled;
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
typename StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::EvalWell
|
|
StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
getQs(const int comp_idx) const
|
|
{
|
|
// Note: currently, the WQTotal definition is still depends on Injector/Producer.
|
|
assert(comp_idx < well_.numComponents());
|
|
|
|
if (well_.isInjector()) { // only single phase injection
|
|
double inj_frac = 0.0;
|
|
switch (well_.wellEcl().injectorType()) {
|
|
case InjectorType::WATER:
|
|
if (comp_idx == int(Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx))) {
|
|
inj_frac = 1.0;
|
|
}
|
|
break;
|
|
case InjectorType::GAS:
|
|
if (Indices::enableSolvent && comp_idx == Indices::contiSolventEqIdx) { // solvent
|
|
inj_frac = well_.wsolvent();
|
|
} else if (comp_idx == int(Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx))) {
|
|
inj_frac = 1.0 - well_.rsRvInj();
|
|
if constexpr (Indices::enableSolvent) {
|
|
inj_frac -= well_.wsolvent();
|
|
}
|
|
} else if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) && comp_idx == int(Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx))) {
|
|
inj_frac = well_.rsRvInj();
|
|
}
|
|
break;
|
|
case InjectorType::OIL:
|
|
if (comp_idx == int(Indices::canonicalToActiveComponentIndex(FluidSystem::oilCompIdx))) {
|
|
inj_frac = 1.0 - well_.rsRvInj();
|
|
} else if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx) && comp_idx == int(Indices::canonicalToActiveComponentIndex(FluidSystem::gasCompIdx))) {
|
|
inj_frac = well_.rsRvInj();
|
|
}
|
|
break;
|
|
case InjectorType::MULTI:
|
|
// Not supported.
|
|
// deferred_logger.warning("MULTI_PHASE_INJECTOR_NOT_SUPPORTED",
|
|
// "Multi phase injectors are not supported, requested for well " + name());
|
|
break;
|
|
}
|
|
return inj_frac * evaluation_[WQTotal];
|
|
} else { // producers
|
|
return evaluation_[WQTotal] * this->volumeFractionScaled(comp_idx);
|
|
}
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
processFractions()
|
|
{
|
|
static constexpr int Water = BlackoilPhases::Aqua;
|
|
static constexpr int Oil = BlackoilPhases::Liquid;
|
|
static constexpr int Gas = BlackoilPhases::Vapour;
|
|
|
|
const auto pu = well_.phaseUsage();
|
|
std::vector<double> F(well_.numPhases(), 0.0);
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
F[pu.phase_pos[Oil]] = 1.0;
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
F[pu.phase_pos[Water]] = value_[WFrac];
|
|
F[pu.phase_pos[Oil]] -= F[pu.phase_pos[Water]];
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
F[pu.phase_pos[Gas]] = value_[GFrac];
|
|
F[pu.phase_pos[Oil]] -= F[pu.phase_pos[Gas]];
|
|
}
|
|
}
|
|
else if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
F[pu.phase_pos[Water]] = 1.0;
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
F[pu.phase_pos[Gas]] = value_[GFrac];
|
|
F[pu.phase_pos[Water]] -= F[pu.phase_pos[Gas]];
|
|
}
|
|
}
|
|
else if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
F[pu.phase_pos[Gas]] = 1.0;
|
|
}
|
|
|
|
[[maybe_unused]] double F_solvent;
|
|
if constexpr (Indices::enableSolvent) {
|
|
F_solvent = value_[SFrac];
|
|
F[pu.phase_pos[Oil]] -= F_solvent;
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
if (F[Water] < 0.0) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
F[pu.phase_pos[Gas]] /= (1.0 - F[pu.phase_pos[Water]]);
|
|
}
|
|
if constexpr (Indices::enableSolvent) {
|
|
F_solvent /= (1.0 - F[pu.phase_pos[Water]]);
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
F[pu.phase_pos[Oil]] /= (1.0 - F[pu.phase_pos[Water]]);
|
|
}
|
|
F[pu.phase_pos[Water]] = 0.0;
|
|
}
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
if (F[pu.phase_pos[Gas]] < 0.0) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
F[pu.phase_pos[Water]] /= (1.0 - F[pu.phase_pos[Gas]]);
|
|
}
|
|
if constexpr (Indices::enableSolvent) {
|
|
F_solvent /= (1.0 - F[pu.phase_pos[Gas]]);
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
F[pu.phase_pos[Oil]] /= (1.0 - F[pu.phase_pos[Gas]]);
|
|
}
|
|
F[pu.phase_pos[Gas]] = 0.0;
|
|
}
|
|
}
|
|
|
|
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
|
|
if (F[pu.phase_pos[Oil]] < 0.0) {
|
|
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
|
|
F[pu.phase_pos[Water]] /= (1.0 - F[pu.phase_pos[Oil]]);
|
|
}
|
|
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
|
|
F[pu.phase_pos[Gas]] /= (1.0 - F[pu.phase_pos[Oil]]);
|
|
}
|
|
if constexpr (Indices::enableSolvent) {
|
|
F_solvent /= (1.0 - F[pu.phase_pos[Oil]]);
|
|
}
|
|
F[pu.phase_pos[Oil]] = 0.0;
|
|
}
|
|
}
|
|
|
|
if constexpr (has_wfrac_variable) {
|
|
value_[WFrac] = F[pu.phase_pos[Water]];
|
|
}
|
|
|
|
if constexpr (has_gfrac_variable) {
|
|
value_[GFrac] = F[pu.phase_pos[Gas]];
|
|
}
|
|
if constexpr (Indices::enableSolvent) {
|
|
value_[SFrac] = F_solvent;
|
|
}
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
double StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
relaxationFactorFractionsProducer(const BVectorWell& dwells) const
|
|
{
|
|
// TODO: not considering solvent yet
|
|
// 0.95 is a experimental value, which remains to be optimized
|
|
double relaxation_factor = 1.0;
|
|
|
|
if (FluidSystem::numActivePhases() > 1) {
|
|
if constexpr (has_wfrac_variable) {
|
|
const double relaxation_factor_w = relaxationFactorFraction(value_[WFrac],
|
|
dwells[0][WFrac]);
|
|
relaxation_factor = std::min(relaxation_factor, relaxation_factor_w);
|
|
}
|
|
|
|
if constexpr (has_gfrac_variable) {
|
|
const double relaxation_factor_g = relaxationFactorFraction(value_[GFrac],
|
|
dwells[0][GFrac]);
|
|
relaxation_factor = std::min(relaxation_factor, relaxation_factor_g);
|
|
}
|
|
|
|
|
|
if constexpr (has_wfrac_variable && has_gfrac_variable) {
|
|
// We need to make sure the even with the relaxation_factor, the sum of F_w and F_g is below one, so there will
|
|
// not be negative oil fraction later
|
|
const double original_sum = value_[WFrac] + value_[GFrac];
|
|
const double relaxed_update = (dwells[0][WFrac] + dwells[0][GFrac]) * relaxation_factor;
|
|
const double possible_updated_sum = original_sum - relaxed_update;
|
|
// We only relax if fraction is above 1.
|
|
// The newton solver should handle the rest
|
|
const double epsilon = 0.001;
|
|
if (possible_updated_sum > 1.0 + epsilon) {
|
|
// since the orignal sum <= 1.0 the epsilon asserts that
|
|
// the relaxed_update is non trivial.
|
|
assert(relaxed_update != 0.);
|
|
|
|
const double further_relaxation_factor = std::abs((1. - original_sum) / relaxed_update) * 0.95;
|
|
relaxation_factor *= further_relaxation_factor;
|
|
}
|
|
}
|
|
assert(relaxation_factor >= 0.0 && relaxation_factor <= 1.0);
|
|
}
|
|
return relaxation_factor;
|
|
}
|
|
|
|
template<class FluidSystem, class Indices, class Scalar>
|
|
void StandardWellPrimaryVariables<FluidSystem,Indices,Scalar>::
|
|
checkFinite(DeferredLogger& deferred_logger) const
|
|
{
|
|
for (const Scalar v : value_) {
|
|
if (!isfinite(v))
|
|
OPM_DEFLOG_THROW(NumericalProblem, "Infinite primary variable after update from wellState well: " << well_.name(), deferred_logger);
|
|
}
|
|
}
|
|
|
|
#define INSTANCE(...) \
|
|
template class StandardWellPrimaryVariables<BlackOilFluidSystem<double,BlackOilDefaultIndexTraits>,__VA_ARGS__,double>;
|
|
|
|
// One phase
|
|
INSTANCE(BlackOilOnePhaseIndices<0u,0u,0u,0u,false,false,0u,1u,0u>)
|
|
INSTANCE(BlackOilOnePhaseIndices<0u,0u,0u,1u,false,false,0u,1u,0u>)
|
|
INSTANCE(BlackOilOnePhaseIndices<0u,0u,0u,0u,false,false,0u,1u,5u>)
|
|
|
|
// Two phase
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,false,0u,0u,0u>)
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,false,0u,1u,0u>)
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,false,0u,2u,0u>)
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,1u,0u,false,false,0u,2u,0u>)
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,1u,0u,false,true,0u,2u,0u>)
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,1u,false,false,0u,1u,0u>)
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,true,0u,0u,0u>)
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,0u,0u,false,true,0u,2u,0u>)
|
|
INSTANCE(BlackOilTwoPhaseIndices<0u,0u,2u,0u,false,false,0u,2u,0u>)
|
|
|
|
// Blackoil
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,0u,false,false,0u,0u>)
|
|
INSTANCE(BlackOilIndices<1u,0u,0u,0u,false,false,0u,0u>)
|
|
INSTANCE(BlackOilIndices<0u,1u,0u,0u,false,false,0u,0u>)
|
|
INSTANCE(BlackOilIndices<0u,0u,1u,0u,false,false,0u,0u>)
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,1u,false,false,0u,0u>)
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,0u,true,false,0u,0u>)
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,0u,false,true,0u,0u>)
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,1u,false,true,0u,0u>)
|
|
INSTANCE(BlackOilIndices<0u,0u,0u,1u,false,false,1u,0u>)
|
|
|
|
}
|