cbb5910a93
the largest change is that all classes below opm/core/props/pvt take the PVT region index as an argument, the higher-level ones (i.e., BlackoilProps*) take cell indices.
163 lines
6.2 KiB
C++
163 lines
6.2 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_PVTDEADSPLINE_HEADER_INCLUDED
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#define OPM_PVTDEADSPLINE_HEADER_INCLUDED
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#include <opm/core/props/pvt/PvtInterface.hpp>
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#include <opm/core/utility/UniformTableLinear.hpp>
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#include <opm/parser/eclipse/Utility/PvdoTable.hpp>
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#include <opm/parser/eclipse/Utility/PvdgTable.hpp>
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#include <vector>
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namespace Opm
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{
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/// Class for immiscible dead oil and dry gas.
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/// The PVT properties can either be given as a function of pressure (p) and surface volume (z)
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/// or pressure (p) 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 PvtDeadSpline : public PvtInterface
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{
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public:
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PvtDeadSpline();
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void initFromOil(Opm::DeckKeywordConstPtr pvdoKeyword,
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int numSamples);
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void initFromGas(Opm::DeckKeywordConstPtr pvdgKeyword,
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int numSamples);
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virtual ~PvtDeadSpline();
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/// Viscosity as a function of p 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* z,
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double* output_mu) const;
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/// Viscosity and its derivatives as a function of p 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* 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 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* 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 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* z,
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double* output_B) const;
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/// Formation volume factor and p-derivative as functions of p 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* 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 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* 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 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* 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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// PVT properties of dry gas or dead oil. We need to store one
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// table per PVT region.
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std::vector<UniformTableLinear<double> > b_;
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std::vector<UniformTableLinear<double> > viscosity_;
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};
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}
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#endif // OPM_PVTDEADSPLINE_HEADER_INCLUDED
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