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fix well model for gasoil thermal

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Tor Harald Sandve 2021-01-21 11:37:25 +01:00
parent 3a0dbdc6e7
commit 036a021c63
5 changed files with 30 additions and 12 deletions
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3
opm/simulators/wells/MultisegmentWell.hpp
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@ -48,6 +48,7 @@ namespace Opm
/// the number of reservior equations
using Base::numEq;
using Base::numPhases;
using Base::has_solvent;
using Base::has_polymer;
@ -69,7 +70,7 @@ namespace Opm
static constexpr int SPres = has_gas + has_water + 1;
// the number of well equations TODO: it should have a more general strategy for it
static const int numWellEq = getPropValue<TypeTag, Properties::EnablePolymer>() ? numEq : numEq + 1;
static const int numWellEq = numPhases + 1;
using typename Base::Scalar;

14
opm/simulators/wells/StandardWell.hpp
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@ -76,6 +76,7 @@ namespace Opm
using GasLiftHandler = Opm::GasLiftRuntime<TypeTag>;
using Base::numEq;
using Base::numPhases;
using Base::has_solvent;
using Base::has_zFraction;
@ -88,16 +89,10 @@ namespace Opm
using FoamModule = Opm::BlackOilFoamModule<TypeTag>;
using BrineModule = Opm::BlackOilBrineModule<TypeTag>;
// polymer concentration and temperature are already known by the well, so
// polymer and energy conservation do not need to be considered explicitly
static const int numPolymerEq = Indices::numPolymers;
static const int numEnergyEq = Indices::numEnergy;
static const int numFoamEq = Indices::numFoam;
static const int numBrineEq = Indices::numBrine;
static const int numExtbos = Indices::numExtbos;
static const int numSolventEq = Indices::numSolvents;
// number of the conservation equations
static const int numWellConservationEq = numEq - numPolymerEq - numEnergyEq - numFoamEq - numBrineEq - numExtbos;
static const int numWellConservationEq = numPhases + numSolventEq;
// number of the well control equations
static const int numWellControlEq = 1;
// number of the well equations that will always be used
@ -113,7 +108,7 @@ namespace Opm
// well control equation is always the last well equation.
// TODO: in the current implementation, we use the well rate as the first primary variables for injectors,
// instead of G_t.
static const bool gasoil = numEq == 2 && (Indices::compositionSwitchIdx >= 0);
static const bool gasoil = numPhases == 2 && (Indices::compositionSwitchIdx >= 0);
static const int WQTotal = 0;
static const int WFrac = gasoil? -1000: 1;
static const int GFrac = gasoil? 1: 2;
@ -331,6 +326,7 @@ namespace Opm
// protected functions from the Base class
using Base::getAllowCrossFlow;
using Base::flowPhaseToEbosCompIdx;
using Base::flowPhaseToEbosPhaseIdx;
using Base::ebosCompIdxToFlowCompIdx;
using Base::wsalt;
using Base::wsolvent;

5
opm/simulators/wells/StandardWell_impl.hpp
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@ -4170,7 +4170,8 @@ namespace Opm
// Note: E100's notion of PI value phase mobility includes
// the reciprocal FVF.
const auto connMob =
mobility[ flowPhaseToEbosCompIdx(p) ].value() * fs.invB(p).value();
mobility[ flowPhaseToEbosCompIdx(p) ].value()
* fs.invB(flowPhaseToEbosPhaseIdx(p)).value();
connPI[p] = connPICalc(connMob);
}
@ -4227,6 +4228,6 @@ namespace Opm
const auto zero = EvalWell { this->numWellEq_ + this->numEq, 0.0 };
const auto mt = std::accumulate(mobility.begin(), mobility.end(), zero);
connII[phase_pos] = connIICalc(mt.value() * fs.invB(phase_pos).value());
connII[phase_pos] = connIICalc(mt.value() * fs.invB(flowPhaseToEbosPhaseIdx(phase_pos)).value());
}
} // namespace Opm

3
opm/simulators/wells/WellInterface.hpp
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@ -85,6 +85,7 @@ namespace Opm
using RateVector = GetPropType<TypeTag, Properties::RateVector>;
static const int numEq = Indices::numEq;
static const int numPhases = Indices::numPhases;
typedef double Scalar;
typedef Dune::FieldVector<Scalar, numEq > VectorBlockType;
@ -434,6 +435,8 @@ namespace Opm
int flowPhaseToEbosCompIdx( const int phaseIdx ) const;
int flowPhaseToEbosPhaseIdx( const int phaseIdx ) const;
int ebosCompIdxToFlowCompIdx( const unsigned compIdx ) const;
double wsolvent() const;

17
opm/simulators/wells/WellInterface_impl.hpp
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@ -297,6 +297,23 @@ namespace Opm
return phaseIdx;
}
template<typename TypeTag>
int
WellInterface<TypeTag>::
flowPhaseToEbosPhaseIdx( const int phaseIdx ) const
{
const auto& pu = phaseUsage();
if (FluidSystem::phaseIsActive(FluidSystem::waterPhaseIdx) && pu.phase_pos[Water] == phaseIdx)
return FluidSystem::waterPhaseIdx;
if (FluidSystem::phaseIsActive(FluidSystem::oilPhaseIdx) && pu.phase_pos[Oil] == phaseIdx)
return FluidSystem::oilPhaseIdx;
if (FluidSystem::phaseIsActive(FluidSystem::gasPhaseIdx) && pu.phase_pos[Gas] == phaseIdx)
return FluidSystem::gasPhaseIdx;
// for other phases return the index
return phaseIdx;
}
template<typename TypeTag>
int
WellInterface<TypeTag>::