0aa7620a0e
instead, we will be going with wrapper classes around the PvtInterface in the next commits. this considerably reduces the amount of copy-and-paste required for temperature support.
188 lines
7.6 KiB
C++
188 lines
7.6 KiB
C++
/*
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Copyright 2010, 2011, 2012 SINTEF ICT, Applied Mathematics.
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This file is part of the Open Porous Media project (OPM).
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OPM is free software: you can redistribute it and/or modify
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it under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 3 of the License, or
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(at your option) any later version.
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OPM is distributed in the hope that it will be useful,
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but WITHOUT ANY WARRANTY; without even the implied warranty of
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MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the
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GNU General Public License for more details.
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You should have received a copy of the GNU General Public License
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along with OPM. If not, see <http://www.gnu.org/licenses/>.
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*/
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#ifndef OPM_PVTLIVEOIL_HEADER_INCLUDED
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#define OPM_PVTLIVEOIL_HEADER_INCLUDED
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#include <opm/core/props/pvt/PvtInterface.hpp>
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#include <opm/parser/eclipse/Deck/Deck.hpp>
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#include <opm/parser/eclipse/EclipseState/EclipseState.hpp>
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#include <vector>
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namespace Opm
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{
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/// Class for miscible live oil (with dissolved gas in liquid phase).
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/// The PVT properties can either be given as a function of pressure (p), temperature (T) and surface volume (z)
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/// or pressure (p), temperature (T) and gas resolution factor (r).
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/// For all the virtual methods, the following apply: p, r and z
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/// are expected to be of size n, size n and n*num_phases, respectively.
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/// Output arrays shall be of size n, and must be valid before
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/// calling the method.
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class PvtLiveOil : public PvtInterface
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{
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public:
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PvtLiveOil(const std::vector<Opm::PvtoTable>& pvtoTables);
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virtual ~PvtLiveOil();
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/// Viscosity as a function of p, T and z.
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virtual void mu(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* T,
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const double* z,
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double* output_mu) const;
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/// Viscosity and its p and r derivatives as a function of p, T and r.
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/// The fluid is considered saturated if r >= rsSat(p).
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virtual void mu(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* T,
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const double* r,
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double* output_mu,
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double* output_dmudp,
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double* output_dmudr) const;
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/// Viscosity as a function of p, T and r.
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/// State condition determined by 'cond'.
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virtual void mu(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* T,
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const double* r,
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const PhasePresence* cond,
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double* output_mu,
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double* output_dmudp,
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double* output_dmudr) const;
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/// Formation volume factor as a function of p, T and z.
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virtual void B(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* T,
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const double* z,
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double* output_B) const;
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/// Formation volume factor and p-derivative as functions of p, T and z.
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virtual void dBdp(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* T,
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const double* z,
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double* output_B,
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double* output_dBdp) const;
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/// The inverse of the formation volume factor b = 1 / B, and its derivatives as a function of p, T and r.
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/// The fluid is considered saturated if r >= rsSat(p).
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virtual void b(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* T,
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const double* r,
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double* output_b,
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double* output_dbdp,
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double* output_dbdr) const;
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/// The inverse of the formation volume factor b = 1 / B, and its derivatives as a function of p, T and r.
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/// State condition determined by 'cond'.
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virtual void b(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* T,
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const double* r,
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const PhasePresence* cond,
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double* output_b,
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double* output_dbdp,
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double* output_dbdr) const;
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/// Solution gas/oil ratio and its derivatives at saturated conditions as a function of p.
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virtual void rsSat(const int n,
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const int* pvtTableIdx,
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const double* p,
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double* output_rsSat,
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double* output_drsSatdp) const;
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/// Vapor oil/gas ratio and its derivatives at saturated conditions as a function of p.
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virtual void rvSat(const int n,
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const int* pvtTableIdx,
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const double* p,
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double* output_rvSat,
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double* output_drvSatdp) const;
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/// Solution factor as a function of p and z.
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virtual void R(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* z,
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double* output_R) const;
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/// Solution factor and p-derivative as functions of p and z.
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virtual void dRdp(const int n,
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const int* pvtTableIdx,
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const double* p,
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const double* z,
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double* output_R,
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double* output_dRdp) const;
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private:
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int getTableIndex_(const int* pvtTableIdx, int cellIdx) const
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{
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if (!pvtTableIdx)
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return 0;
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return pvtTableIdx[cellIdx];
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}
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double evalB(size_t pvtTableIdx, double press, const double* surfvol) const;
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void evalBDeriv(size_t pvtTableIdx, double press, const double* surfvol, double& B, double& dBdp) const;
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double evalR(size_t pvtTableIdx, double press, const double* surfvol) const;
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void evalRDeriv(size_t pvtTableIdx, double press, const double* surfvol, double& R, double& dRdp) const;
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// item: 1=>1/B 2=>mu;
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double miscible_oil(const double press,
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const double* surfvol,
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const int pvtTableIdx,
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const int item,
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const bool deriv = false) const;
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double miscible_oil(const double press,
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const double r,
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const int pvtTableIdx,
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const int item,
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const int deriv = 0) const;
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double miscible_oil(const double press,
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const double r,
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const PhasePresence& cond,
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const int pvtTableIdx,
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const int item,
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const int deriv = 0) const;
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// PVT properties of live oil (with dissolved gas). We need to
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// store one table per PVT region.
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std::vector<std::vector<std::vector<double> > > saturated_oil_table_;
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std::vector<std::vector<std::vector<std::vector<double> > > > undersat_oil_tables_;
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};
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}
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#endif // OPM_PVTLIVEOIL_HEADER_INCLUDED
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