StandardWellPrimaryVariables.hpp

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/*
  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/>.
*/
 
 
#ifndef OPM_STANDARDWELL_PRIMARY_VARIABLES_HEADER_INCLUDED
#define OPM_STANDARDWELL_PRIMARY_VARIABLES_HEADER_INCLUDED
 
#include <opm/material/densead/Evaluation.hpp>
 
#include <opm/simulators/wells/StandardWellEquations.hpp>
 
#include <string_view>
#include <vector>
 
namespace Opm
{
 
class DeferredLogger;
template<class FluidSystem, class Indices> class WellInterfaceIndices;
template<typename Scalar, typename IndexTraits> class WellState;
 
template<class FluidSystem, class Indices>
class StandardWellPrimaryVariables {
protected:
    // the positions of the primary variables for StandardWell
    // the first one is the weighted total rate (WQ_t), the second and the third ones are F_w and F_g,
    // which represent the fraction of Water and Gas based on the weighted total rate, the last one is BHP.
    // correspondingly, we have four well equations for blackoil model, the first three are mass
    // converstation equations, and the last one is the well control equation.
    // primary variables related to other components, will be before the Bhp and after F_g.
    // 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.
 
    // Table showing the primary variable indices, depending on what phases are present:
    //
    //         WOG     OG     WG     WO    W/O/G (single phase)
    // WQTotal   0      0      0      0                       0
    // WFrac     1  -1000     -1000   1                   -1000
    // GFrac     2      1      1  -1000                   -1000
    // Spres     3      2      2      2                       1
 
    static constexpr int numWellControlEq = 1;
 
public:
    static constexpr int numWellConservationEq = Indices::numPhases + Indices::numSolvents;
 
    static constexpr int numStaticWellEq = numWellConservationEq + numWellControlEq;
 
    static constexpr int WQTotal = 0; 
 
    static constexpr int Bhp = numStaticWellEq - numWellControlEq;
 
    static constexpr bool has_wfrac_variable = Indices::waterEnabled && Indices::oilEnabled;
    static constexpr bool has_gfrac_variable = Indices::gasEnabled && Indices::numPhases > 1;
    static constexpr int WFrac = has_wfrac_variable ? 1 : -1000;
    static constexpr int GFrac = has_gfrac_variable ? has_wfrac_variable + 1 : -1000;
    static constexpr int SFrac = !Indices::enableSolvent ? -1000 : has_wfrac_variable+has_gfrac_variable+1;
 
    using Scalar = typename FluidSystem::Scalar;
    using IndexTraits = typename FluidSystem::IndexTraitsType;
    using EvalWell = DenseAd::DynamicEvaluation<Scalar, numStaticWellEq + Indices::numEq + 1>;
    using BVectorWell = typename StandardWellEquations<Scalar, IndexTraits, Indices::numEq>::BVectorWell;
 
    explicit StandardWellPrimaryVariables(const WellInterfaceIndices<FluidSystem,Indices>& well)
        : well_(well)
    {}
 
    void resize(const int numWellEq);
 
    int numWellEq() const { return numWellEq_; }
 
    void update(const WellState<Scalar, IndexTraits>& well_state,
                const bool stop_or_zero_rate_target,
                DeferredLogger& deferred_logger);
 
    void updatePolyMW(const WellState<Scalar, IndexTraits>& well_state);
 
    void updateNewton(const BVectorWell& dwells,
                      const bool stop_or_zero_rate_target,
                      const Scalar dFLimit,
                      const Scalar dBHPLimit,
                      DeferredLogger& deferred_logger);
 
    void updateNewtonPolyMW(const BVectorWell& dwells);
 
    void checkFinite(DeferredLogger& deferred_logger, std::string_view context) const;
 
    void copyToWellState(WellState<Scalar, IndexTraits>& well_state,
                         DeferredLogger& deferred_logger) const;
 
    void copyToWellStatePolyMW(WellState<Scalar, IndexTraits>& well_state) const;
 
    EvalWell volumeFractionScaled(const int compIdx) const;
 
    EvalWell surfaceVolumeFraction(const int compIdx) const;
 
    EvalWell getQs(const int compIdx) const;
 
    Scalar value(const int idx) const
    { return value_[idx]; }
 
    const EvalWell& eval(const int idx) const
    { return evaluation_[idx]; }
 
    void setValue(const int idx, const Scalar val)
    { value_[idx] = val; }
 
private:
    void setEvaluationsFromValues();
 
    Scalar relaxationFactorFractionsProducer(const BVectorWell& dwells,
                                             DeferredLogger& deferred_logger) const;
 
    EvalWell volumeFraction(const int compIdx) const;
 
    void processFractions();
 
    std::vector<Scalar> value_;
 
    std::vector<EvalWell> evaluation_;
 
    const WellInterfaceIndices<FluidSystem,Indices>& well_; 
 
    int numWellEq_ = numStaticWellEq;
};
 
}
 
#endif // OPM_STANDARDWELL_PRIMARY_VARIABLES_HEADER_INCLUDED