Enable single-phase runs.

This commit is contained in:
Halvor M. Nilsen 2019-10-09 15:24:23 +02:00 committed by Atgeirr Flø Rasmussen
parent e4e8425bad
commit d873ae165d
12 changed files with 264 additions and 171 deletions

View File

@ -395,7 +395,16 @@ public:
}
if (oilPressure_.size() > 0) {
oilPressure_[globalDofIdx] = Opm::getValue(fs.pressure(oilPhaseIdx));
if (FluidSystem::phaseIsActive(oilPhaseIdx)) {
oilPressure_[globalDofIdx] = Opm::getValue(fs.pressure(oilPhaseIdx));
}else{
// put pressure in oil pressure for output
if (FluidSystem::phaseIsActive(waterPhaseIdx)) {
oilPressure_[globalDofIdx] = Opm::getValue(fs.pressure(waterPhaseIdx));
} else {
oilPressure_[globalDofIdx] = Opm::getValue(fs.pressure(gasPhaseIdx));
}
}
Opm::Valgrind::CheckDefined(oilPressure_[globalDofIdx]);
}

View File

@ -665,17 +665,20 @@ public:
minTimeStepSize_ = tuning.getTSMINZ(0);
}
initFluidSystem_();
// deal with DRSDT
unsigned ntpvt = eclState.runspec().tabdims().getNumPVTTables();
maxDRs_.resize(ntpvt, 1e30);
dRsDtOnlyFreeGas_.resize(ntpvt, false);
size_t numDof = this->model().numGridDof();
lastRs_.resize(numDof, 0.0);
maxDRv_.resize(ntpvt, 1e30);
lastRv_.resize(numDof, 0.0);
maxOilSaturation_.resize(numDof, 0.0);
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
maxDRs_.resize(ntpvt, 1e30);
dRsDtOnlyFreeGas_.resize(ntpvt, false);
lastRs_.resize(numDof, 0.0);
maxDRv_.resize(ntpvt, 1e30);
lastRv_.resize(numDof, 0.0);
maxOilSaturation_.resize(numDof, 0.0);
}
initFluidSystem_();
updateElementDepths_();
readRockParameters_();
readMaterialParameters_();

View File

@ -54,14 +54,9 @@ namespace Opm
}
}
// Only 2 or 3 phase systems handled.
if (pu.num_phases < 2 || pu.num_phases > 3) {
OPM_THROW(std::runtime_error, "Cannot handle cases with " << pu.num_phases << " phases.");
}
// We need oil systems, since we do not support the keywords needed for
// water-gas systems.
if (!pu.phase_used[BlackoilPhases::Liquid]) {
if (!pu.phase_used[BlackoilPhases::Liquid] && !(pu.num_phases == 1)) {
OPM_THROW(std::runtime_error, "Cannot handle cases with no OIL, i.e. water-gas systems.");
}

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@ -422,29 +422,34 @@ namespace Opm {
Scalar saturationsOld[FluidSystem::numPhases] = { 0.0 };
Scalar oilSaturationOld = 1.0;
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
saturationsOld[FluidSystem::waterPhaseIdx] = priVarsOld[Indices::waterSaturationIdx];
oilSaturationOld -= saturationsOld[FluidSystem::waterPhaseIdx];
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx) && priVarsOld.primaryVarsMeaning() == PrimaryVariables::Sw_po_Sg) {
saturationsOld[FluidSystem::gasPhaseIdx] = priVarsOld[Indices::compositionSwitchIdx];
oilSaturationOld -= saturationsOld[FluidSystem::gasPhaseIdx];
}
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
saturationsOld[FluidSystem::oilPhaseIdx] = oilSaturationOld;
}
if (FluidSystem::numActivePhases() > 1) {
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
saturationsOld[FluidSystem::waterPhaseIdx] = priVarsOld[Indices::waterSaturationIdx];
oilSaturationOld -= saturationsOld[FluidSystem::waterPhaseIdx];
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx) &&
priVarsOld.primaryVarsMeaning() == PrimaryVariables::Sw_po_Sg)
{
saturationsOld[FluidSystem::gasPhaseIdx] = priVarsOld[Indices::compositionSwitchIdx];
oilSaturationOld -= saturationsOld[FluidSystem::gasPhaseIdx];
}
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx)) {
saturationsOld[FluidSystem::oilPhaseIdx] = oilSaturationOld;
}
for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++ phaseIdx) {
Scalar tmp = saturationsNew[phaseIdx] - saturationsOld[phaseIdx];
resultDelta += tmp*tmp;
resultDenom += saturationsNew[phaseIdx]*saturationsNew[phaseIdx];
assert(std::isfinite(resultDelta));
assert(std::isfinite(resultDenom));
}
}
// NB fix me! adding pressures changes to satutation changes does not make sense
Scalar tmp = pressureNew - pressureOld;
resultDelta += tmp*tmp;
resultDenom += pressureNew*pressureNew;
for (unsigned phaseIdx = 0; phaseIdx < FluidSystem::numPhases; ++ phaseIdx) {
const Scalar tmpSat = saturationsNew[phaseIdx] - saturationsOld[phaseIdx];
resultDelta += tmpSat * tmpSat;
resultDenom += saturationsNew[phaseIdx]*saturationsNew[phaseIdx];
}
}
resultDelta = gridView.comm().sum(resultDelta);

View File

@ -60,6 +60,7 @@ AdaptiveSimulatorTimer& AdaptiveSimulatorTimer::operator++ ()
{
++current_step_;
current_time_ += dt_;
assert(dt_ > 0);
// store used time step sizes
steps_.push_back( dt_ );
return *this;
@ -71,7 +72,7 @@ AdaptiveSimulatorTimer& AdaptiveSimulatorTimer::operator++ ()
double remaining = (total_time_ - current_time_);
// apply max time step if it was set
dt_ = std::min( dt_estimate, max_time_step_ );
assert(dt_ > 0);
if( remaining > 0 ) {
// set new time step (depending on remaining time)
@ -81,6 +82,7 @@ AdaptiveSimulatorTimer& AdaptiveSimulatorTimer::operator++ ()
if( dt_ > max_time_step_ ) {
dt_ = 0.5 * remaining;
}
assert(dt_ > 0);
return;
}
@ -89,6 +91,7 @@ AdaptiveSimulatorTimer& AdaptiveSimulatorTimer::operator++ ()
if( 1.5 * dt_ > remaining ) {
dt_ = 0.5 * remaining;
assert(dt_ > 0);
return;
}
}
@ -102,6 +105,7 @@ AdaptiveSimulatorTimer& AdaptiveSimulatorTimer::operator++ ()
double AdaptiveSimulatorTimer::currentStepLength () const
{
assert(dt_ > 0);
return dt_;
}

View File

@ -293,9 +293,10 @@ namespace Opm {
double dtEstimate = timeStepControl_->computeTimeStepSize(dt, iterations, relativeChange,
substepTimer.simulationTimeElapsed());
assert(dtEstimate > 0);
// limit the growth of the timestep size by the growth factor
dtEstimate = std::min(dtEstimate, double(maxGrowth_ * dt));
assert(dtEstimate > 0);
// further restrict time step size growth after convergence problems
if (restarts > 0) {
dtEstimate = std::min(growthFactor_ * dt, dtEstimate);
@ -309,7 +310,7 @@ namespace Opm {
const double maxPredictionTHPTimestep = 16.0 * unit::day;
dtEstimate = std::min(dtEstimate, maxPredictionTHPTimestep);
}
assert(dtEstimate > 0);
if (timestepVerbose_) {
std::ostringstream ss;
substepReport.reportStep(ss);

View File

@ -128,13 +128,17 @@ namespace Opm
{
// shift errors
for( int i=0; i<2; ++i ) {
errors_[ i ] = errors_[i+1];
errors_[ i ] = errors_[i+1];
}
// store new error
const double error = relChange.relativeChange();
errors_[ 2 ] = error;
for( int i=0; i<2; ++i ) {
assert(std::isfinite(errors_[i]));
assert(errors_[i]>0);
}
if( error > tol_ )
{
// adjust dt by given tolerance

View File

@ -251,9 +251,19 @@ namespace Opm {
const unsigned cellIdx = elemCtx.globalSpaceIndex(/*spaceIdx=*/0, /*timeIdx=*/0);
const auto& intQuants = elemCtx.intensiveQuantities(/*spaceIdx=*/0, /*timeIdx=*/0);
const auto& fs = intQuants.fluidState();
const double p = fs.pressure(FluidSystem::oilPhaseIdx).value();
cellPressures[cellIdx] = p;
// copy of get perfpressure in Standard well
// exept for value
double perf_pressure = 0.0;
if (Indices::oilEnabled) {
perf_pressure = fs.pressure(FluidSystem::oilPhaseIdx).value();
} else {
if (Indices::waterEnabled) {
perf_pressure = fs.pressure(FluidSystem::waterPhaseIdx).value();
} else {
perf_pressure = fs.pressure(FluidSystem::gasPhaseIdx).value();
}
}
cellPressures[cellIdx] = perf_pressure;
}
well_state_.init(wells(), cellPressures, schedule(), wells_ecl_, timeStepIdx, &previous_well_state_, phase_usage_);
@ -1525,8 +1535,8 @@ namespace Opm {
int
BlackoilWellModel<TypeTag>::numComponents() const
{
if (numPhases() == 2) {
return 2;
if (numWells() > 0 && numPhases() < 3) {
return numPhases();
}
int numComp = FluidSystem::numComponents;
if (has_solvent_) {

View File

@ -493,11 +493,13 @@ namespace Opm {
// sum p, rs, rv, and T.
double hydrocarbonPV = pv_cell*hydrocarbon;
pv += hydrocarbonPV;
p += fs.pressure(FluidSystem::oilPhaseIdx).value()*hydrocarbonPV;
rs += fs.Rs().value()*hydrocarbonPV;
rv += fs.Rv().value()*hydrocarbonPV;
T += fs.temperature(FluidSystem::oilPhaseIdx).value()*hydrocarbonPV;
if (hydrocarbonPV > 0) {
pv += hydrocarbonPV;
p += fs.pressure(FluidSystem::oilPhaseIdx).value()*hydrocarbonPV;
rs += fs.Rs().value()*hydrocarbonPV;
rv += fs.Rv().value()*hydrocarbonPV;
T += fs.temperature(FluidSystem::oilPhaseIdx).value()*hydrocarbonPV;
}
}
for (const auto& reg : rmap_.activeRegions()) {

View File

@ -59,6 +59,7 @@ namespace Opm
using typename Base::Indices;
using typename Base::RateConverterType;
using typename Base::SparseMatrixAdapter;
using typename Base::FluidState;
using Base::numEq;
@ -293,6 +294,8 @@ namespace Opm
EvalWell extendEval(const Eval& in) const;
Eval getPerfPressure(const FluidState& fs) const;
// xw = inv(D)*(rw - C*x)
void recoverSolutionWell(const BVector& x, BVectorWell& xw) const;

View File

@ -238,6 +238,10 @@ namespace Opm
StandardWell<TypeTag>::
wellVolumeFraction(const unsigned compIdx) const
{
if (FluidSystem::numActivePhases() == 1) {
return EvalWell(numWellEq_ + numEq, 1.0);
}
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx) && compIdx == Indices::canonicalToActiveComponentIndex(FluidSystem::waterCompIdx)) {
return primary_variables_evaluation_[WFrac];
}
@ -305,6 +309,24 @@ namespace Opm
template<typename TypeTag>
typename StandardWell<TypeTag>::Eval
StandardWell<TypeTag>::getPerfPressure(const typename StandardWell<TypeTag>::FluidState& fs) const
{
Eval pressure;
if (Indices::oilEnabled) {
pressure = fs.pressure(FluidSystem::oilPhaseIdx);
} else {
if (Indices::waterEnabled) {
pressure = fs.pressure(FluidSystem::waterPhaseIdx);
} else {
pressure = fs.pressure(FluidSystem::gasPhaseIdx);
}
}
return pressure;
}
template<typename TypeTag>
void
StandardWell<TypeTag>::
@ -321,7 +343,7 @@ namespace Opm
{
const auto& fs = intQuants.fluidState();
const EvalWell pressure = extendEval(fs.pressure(FluidSystem::oilPhaseIdx));
const EvalWell pressure = extendEval(getPerfPressure(fs));
const EvalWell rs = extendEval(fs.Rs());
const EvalWell rv = extendEval(fs.Rv());
std::vector<EvalWell> b_perfcells_dense(num_components_, EvalWell{numWellEq_ + numEq, 0.0});
@ -669,7 +691,9 @@ namespace Opm
|| (pu.phase_pos[Gas] == p && summaryConfig.hasSummaryKey("WPIG:" + name()))) {
const unsigned int compIdx = flowPhaseToEbosCompIdx(p);
const double drawdown = well_state.perfPress()[first_perf_ + perf] - intQuants.fluidState().pressure(FluidSystem::oilPhaseIdx).value();
const auto& fs = intQuants.fluidState();
Eval perf_pressure = getPerfPressure(fs);
const double drawdown = well_state.perfPress()[first_perf_ + perf] - perf_pressure.value();
const bool new_well = schedule.hasWellEvent(name(), ScheduleEvents::NEW_WELL, current_step_);
double productivity_index = cq_s[compIdx].value() / drawdown;
scaleProductivityIndex(perf, productivity_index, new_well, deferred_logger);
@ -679,12 +703,15 @@ namespace Opm
}
// add vol * dF/dt + Q to the well equations;
for (int componentIdx = 0; componentIdx < numWellConservationEq; ++componentIdx) {
// TODO: following the development in MSW, we need to convert the volume of the wellbore to be surface volume
// since all the rates are under surface condition
EvalWell resWell_loc = (wellSurfaceVolumeFraction(componentIdx) - F0_[componentIdx]) * volume / dt;
EvalWell resWell_loc(numWellEq_ + numEq, 0.0);
if (FluidSystem::numActivePhases() > 1) {
assert(dt > 0);
resWell_loc += (wellSurfaceVolumeFraction(componentIdx) - F0_[componentIdx]) * volume / dt;
}
resWell_loc -= getQs(componentIdx) * well_efficiency_factor_;
for (int pvIdx = 0; pvIdx < numWellEq_; ++pvIdx) {
invDuneD_[0][0][componentIdx][pvIdx] += resWell_loc.derivative(pvIdx+numEq);
@ -919,29 +946,30 @@ namespace Opm
const double relaxation_factor_fractions = (well_type_ == PRODUCER) ?
relaxationFactorFractionsProducer(old_primary_variables, dwells)
: 1.0;
if (FluidSystem::numActivePhases() > 1) {
// update the second and third well variable (The flux fractions)
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
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);
// primary_variables_[WFrac] = old_primary_variables[WFrac] - dx2_limited;
primary_variables_[WFrac] = old_primary_variables[WFrac] - dx2_limited;
}
// update the second and third well variable (The flux fractions)
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
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);
// primary_variables_[WFrac] = old_primary_variables[WFrac] - dx2_limited;
primary_variables_[WFrac] = old_primary_variables[WFrac] - dx2_limited;
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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);
primary_variables_[GFrac] = old_primary_variables[GFrac] - dx3_limited;
}
if (has_solvent) {
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);
primary_variables_[SFrac] = old_primary_variables[SFrac] - dx4_limited;
}
processFractions();
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
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);
primary_variables_[GFrac] = old_primary_variables[GFrac] - dx3_limited;
}
if (has_solvent) {
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);
primary_variables_[SFrac] = old_primary_variables[SFrac] - dx4_limited;
}
processFractions();
// updating the total rates Q_t
const double relaxation_factor_rate = relaxationFactorRate(old_primary_variables, dwells);
primary_variables_[WQTotal] = old_primary_variables[WQTotal] - dwells[0][WQTotal] * relaxation_factor_rate;
@ -956,6 +984,10 @@ namespace Opm
}
updateExtraPrimaryVariables(dwells);
for (int i = 0; i < primary_variables_.size(); ++i) {
assert(Opm::isfinite(primary_variables_[i]));
}
}
@ -1073,49 +1105,53 @@ namespace Opm
updateWellStateFromPrimaryVariables(WellState& well_state, Opm::DeferredLogger& deferred_logger) const
{
const PhaseUsage& pu = phaseUsage();
assert( FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) );
const int oil_pos = pu.phase_pos[Oil];
std::vector<double> F(number_of_phases_, 0.0);
F[oil_pos] = 1.0;
if (FluidSystem::numActivePhases() == 1) {
F[0] = 1.0;
} else {
assert( 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] = primary_variables_[WFrac];
F[oil_pos] -= F[water_pos];
}
if ( FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx) ) {
const int gas_pos = pu.phase_pos[Gas];
F[gas_pos] = primary_variables_[GFrac];
F[oil_pos] -= F[gas_pos];
}
double F_solvent = 0.0;
if (has_solvent) {
F_solvent = primary_variables_[SFrac];
F[oil_pos] -= F_solvent;
}
// convert the fractions to be Q_p / G_total to calculate the phase rates
for (int p = 0; p < number_of_phases_; ++p) {
const double scal = 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.;
if ( FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx) ) {
const int water_pos = pu.phase_pos[Water];
F[water_pos] = primary_variables_[WFrac];
F[oil_pos] -= F[water_pos];
}
}
// 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 (has_solvent){
F_solvent /= scalingFactor(contiSolventEqIdx);
F[pu.phase_pos[Gas]] += F_solvent;
}
if ( FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx) ) {
const int gas_pos = pu.phase_pos[Gas];
F[gas_pos] = primary_variables_[GFrac];
F[oil_pos] -= F[gas_pos];
}
double F_solvent = 0.0;
if (has_solvent) {
F_solvent = primary_variables_[SFrac];
F[oil_pos] -= F_solvent;
}
// convert the fractions to be Q_p / G_total to calculate the phase rates
for (int p = 0; p < number_of_phases_; ++p) {
const double scal = 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 (has_solvent){
F_solvent /= scalingFactor(contiSolventEqIdx);
F[pu.phase_pos[Gas]] += F_solvent;
}
}
well_state.bhp()[index_of_well_] = primary_variables_[Bhp];
// calculate the phase rates based on the primary variables
@ -1292,6 +1328,10 @@ namespace Opm
break;
} // end of switch
for (int i = 0; i < primary_variables_.size(); ++i) {
assert(Opm::isfinite(primary_variables_[i]));
}
}
@ -1324,7 +1364,8 @@ namespace Opm
const auto& int_quantities = *(ebos_simulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/ 0));
const auto& fs = int_quantities.fluidState();
// the pressure of the reservoir grid block the well connection is in
const double p_r = fs.pressure(FluidSystem::oilPhaseIdx).value();
Eval perf_pressure = getPerfPressure(fs);
double p_r = perf_pressure.value();
// calculating the b for the connection
std::vector<double> b_perf(num_components_);
@ -1550,8 +1591,9 @@ namespace Opm
const int cell_idx = well_cells_[perf];
const auto& intQuants = *(ebos_simulator.model().cachedIntensiveQuantities(cell_idx, /*timeIdx=*/0));
const auto& fs = intQuants.fluidState();
Eval perf_pressure = getPerfPressure(fs);
const double pressure = perf_pressure.value();
const double pressure = (fs.pressure(FluidSystem::oilPhaseIdx)).value();
const double bhp = getBhp().value();
// Pressure drawdown (also used to determine direction of flow)
@ -1755,6 +1797,7 @@ namespace Opm
// TODO: to check why should be perf - 1
const double p_above = perf == 0 ? well_state.bhp()[w] : well_state.perfPress()[first_perf_ + perf - 1];
const double p_avg = (well_state.perfPress()[first_perf_ + perf] + p_above)/2;
// strange choice
const double temperature = fs.temperature(FluidSystem::oilPhaseIdx).value();
if (waterPresent) {
@ -2518,57 +2561,57 @@ namespace Opm
}
}
if (std::abs(total_well_rate) > 0.) {
const auto pu = phaseUsage();
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
primary_variables_[WFrac] = scalingFactor(pu.phase_pos[Water]) * well_state.wellRates()[np*well_index + pu.phase_pos[Water]] / total_well_rate;
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
primary_variables_[GFrac] = scalingFactor(pu.phase_pos[Gas]) * (well_state.wellRates()[np*well_index + pu.phase_pos[Gas]] - well_state.solventWellRate(well_index)) / total_well_rate ;
}
if (has_solvent) {
primary_variables_[SFrac] = scalingFactor(pu.phase_pos[Gas]) * well_state.solventWellRate(well_index) / total_well_rate ;
}
} else { // total_well_rate == 0
if (well_type_ == INJECTOR) {
auto phase = well_ecl_.getInjectionProperties().injectorType;
// only single phase injection handled
if (FluidSystem::numActivePhases() > 1) {
if (std::abs(total_well_rate) > 0.) {
const auto pu = phaseUsage();
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
if (phase == Well2::InjectorType::WATER) {
primary_variables_[WFrac] = 1.0;
} else {
primary_variables_[WFrac] = 0.0;
}
primary_variables_[WFrac] = scalingFactor(pu.phase_pos[Water]) * well_state.wellRates()[np*well_index + pu.phase_pos[Water]] / total_well_rate;
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
if (phase == Well2::InjectorType::GAS) {
primary_variables_[GFrac] = 1.0 - wsolvent();
if (has_solvent) {
primary_variables_[SFrac] = wsolvent();
primary_variables_[GFrac] = scalingFactor(pu.phase_pos[Gas]) * (well_state.wellRates()[np*well_index + pu.phase_pos[Gas]] - well_state.solventWellRate(well_index)) / total_well_rate ;
}
if (has_solvent) {
primary_variables_[SFrac] = scalingFactor(pu.phase_pos[Gas]) * well_state.solventWellRate(well_index) / total_well_rate ;
}
} else { // total_well_rate == 0
if (well_type_ == INJECTOR) {
auto phase = well_ecl_.getInjectionProperties().injectorType;
// only single phase injection handled
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
if (phase == Well2::InjectorType::WATER) {
primary_variables_[WFrac] = 1.0;
} else {
primary_variables_[WFrac] = 0.0;
}
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
if (phase == Well2::InjectorType::GAS) {
primary_variables_[GFrac] = 1.0 - wsolvent();
if (has_solvent) {
primary_variables_[SFrac] = wsolvent();
}
} else {
primary_variables_[GFrac] = 0.0;
}
} else {
primary_variables_[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_type_ == PRODUCER) { // producers
// TODO: the following are not addressed for the solvent case yet
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
primary_variables_[WFrac] = 1.0 / np;
// 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_type_ == PRODUCER) { // producers
// TODO: the following are not addressed for the solvent case yet
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
primary_variables_[WFrac] = 1.0 / np;
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
primary_variables_[GFrac] = 1.0 / np;
}
} else {
OPM_DEFLOG_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well", deferred_logger);
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
primary_variables_[GFrac] = 1.0 / np;
}
} else {
OPM_DEFLOG_THROW(std::logic_error, "Expected PRODUCER or INJECTOR type of well", deferred_logger);
}
}
// BHP
primary_variables_[Bhp] = well_state.bhp()[index_of_well_];
@ -2579,6 +2622,10 @@ namespace Opm
primary_variables_[Bhp + 1 + number_of_perforations_ + perf] = well_state.perfSkinPressure()[first_perf_ + perf];
}
}
for (int i = 0; i < primary_variables_.size(); ++i) {
assert(Opm::isfinite(primary_variables_[i]));
}
}
@ -2824,28 +2871,31 @@ namespace Opm
// 0.95 is a experimental value, which remains to be optimized
double relaxation_factor = 1.0;
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
const double relaxation_factor_w = relaxationFactorFraction(primary_variables[WFrac], dwells[0][WFrac]);
relaxation_factor = std::min(relaxation_factor, relaxation_factor_w);
}
if (FluidSystem::numActivePhases() > 1) {
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)) {
const double relaxation_factor_w = relaxationFactorFraction(primary_variables[WFrac], dwells[0][WFrac]);
relaxation_factor = std::min(relaxation_factor, relaxation_factor_w);
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
const double relaxation_factor_g = relaxationFactorFraction(primary_variables[GFrac], dwells[0][GFrac]);
relaxation_factor = std::min(relaxation_factor, relaxation_factor_g);
}
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
const double relaxation_factor_g = relaxationFactorFraction(primary_variables[GFrac], dwells[0][GFrac]);
relaxation_factor = std::min(relaxation_factor, relaxation_factor_g);
}
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx) && FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
// 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 = primary_variables[WFrac] + primary_variables[GFrac];
const double relaxed_update = (dwells[0][WFrac] + dwells[0][GFrac]) * relaxation_factor;
const double possible_updated_sum = original_sum - relaxed_update;
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx)
&& FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx)) {
// 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 = primary_variables[WFrac] + primary_variables[GFrac];
const double relaxed_update = (dwells[0][WFrac] + dwells[0][GFrac]) * relaxation_factor;
const double possible_updated_sum = original_sum - relaxed_update;
if (possible_updated_sum > 1.0) {
assert(relaxed_update != 0.);
if (possible_updated_sum > 1.0) {
assert(relaxed_update != 0.);
const double further_relaxation_factor = std::abs((1. - original_sum) / relaxed_update) * 0.95;
relaxation_factor *= further_relaxation_factor;
const double further_relaxation_factor = std::abs((1. - original_sum) / relaxed_update) * 0.95;
relaxation_factor *= further_relaxation_factor;
}
}
}

View File

@ -94,6 +94,7 @@ namespace Opm
static const bool has_solvent = GET_PROP_VALUE(TypeTag, EnableSolvent);
static const bool has_polymer = GET_PROP_VALUE(TypeTag, EnablePolymer);
static const bool has_energy = GET_PROP_VALUE(TypeTag, EnableEnergy);
static const bool has_temperature = GET_PROP_VALUE(TypeTag, EnableTemperature);
// flag for polymer molecular weight related
static const bool has_polymermw = GET_PROP_VALUE(TypeTag, EnablePolymerMW);
static const bool has_foam = GET_PROP_VALUE(TypeTag, EnableFoam);
@ -106,7 +107,13 @@ namespace Opm
// For the conversion between the surface volume rate and reservoir voidage rate
using RateConverterType = RateConverter::
SurfaceToReservoirVoidage<FluidSystem, std::vector<int> >;
static const bool compositionSwitchEnabled = Indices::gasEnabled;
using FluidState = Opm::BlackOilFluidState<Eval,
FluidSystem,
has_temperature,
has_energy,
compositionSwitchEnabled,
Indices::numPhases >;
/// Constructor
WellInterface(const Well2& well, const int time_step, const Wells* wells,
const ModelParameters& param,