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Make it possible to combine solvent and RESV

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Compute the conversion factor for solvent using the RateConverter.hpp
This commit is contained in:
Tor Harald Sandve
2017-11-22 14:39:42 +01:00
parent f2a51d29e7
commit 054361d537
7 changed files with 98 additions and 24 deletions
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37
opm/autodiff/StandardWell_impl.hpp
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@@ -24,13 +24,18 @@ namespace Opm
{
template<typename TypeTag>
StandardWell<TypeTag>::
StandardWell(const Well* well, const int time_step, const Wells* wells, const ModelParameters& param)
StandardWell(const Well* well, const int time_step, const Wells* wells,
const ModelParameters& param,
const RateConverterType& rate_converter,
const int pvtRegionIdx)
: Base(well, time_step, wells, param)
, perf_densities_(number_of_perforations_)
, perf_pressure_diffs_(number_of_perforations_)
, primary_variables_(numWellEq, 0.0)
, primary_variables_evaluation_(numWellEq) // the number of the primary variables
, F0_(numWellEq)
, rateConverter_(rate_converter)
, pvtRegionIdx_(pvtRegionIdx)
{
duneB_.setBuildMode( OffDiagMatWell::row_wise );
duneC_.setBuildMode( OffDiagMatWell::row_wise );
@@ -861,13 +866,7 @@ namespace Opm
primary_variables_[SFrac] = F_solvent;
}
// 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[pu.phase_pos[Gas]] += F_solvent;
}
// The interpretation of the first well variable depends on the well control
// The interpretation of the first well variable depends on the well control
const WellControls* wc = well_controls_;
// TODO: we should only maintain one current control either from the well_state or from well_controls struct.
@@ -884,6 +883,18 @@ namespace Opm
}
}
// 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){
const double scal = scalingFactor(contiSolventEqIdx);
if (scal > 0) {
F_solvent /= scal ;
} else {
F_solvent = 0.;
}
F[pu.phase_pos[Gas]] += F_solvent;
}
switch (well_controls_iget_type(wc, current)) {
case THP: // The BHP and THP both uses the total rate as first well variable.
case BHP:
@@ -1981,9 +1992,13 @@ namespace Opm
const double* distr = well_controls_get_current_distr(wc);
if (well_controls_get_current_type(wc) == RESERVOIR_RATE) {
if (has_solvent && phaseIdx == contiSolventEqIdx )
OPM_THROW(std::runtime_error, "RESERVOIR_RATE control in combination with solvent is not implemented");
if (has_solvent && phaseIdx == contiSolventEqIdx ) {
typedef Ewoms::BlackOilSolventModule<TypeTag> SolventModule;
double coeff = 0;
rateConverter_.template calcCoeffSolvent<SolventModule>(0, pvtRegionIdx_, coeff);
return coeff;
}
// TODO: use the rateConverter here as well.
return distr[phaseIdx];
}
const auto& pu = phaseUsage();