mirror of
https://github.com/OPM/opm-simulators.git
synced 2025-02-25 18:55:30 -06:00
because fluid-matrix interactions have been independent of the number of phases for a while. The only law left in this folder (implementing the Parker-van Genuchten law) has been moved one folder up and been cleaned up considerably.
486 lines
17 KiB
C++
486 lines
17 KiB
C++
/*
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Copyright (C) 2008-2013 by Andreas Lauser
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Copyright (C) 2012 by Holger Class
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Copyright (C) 2012 by Vishal Jambhekar
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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 2 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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/*!
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* \file
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* \copydoc Opm::ThreePhaseParkerVanGenuchten
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*/
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#ifndef OPM_THREE_PHASE_PARKER_VAN_GENUCHTEN_HPP
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#define OPM_THREE_PHASE_PARKER_VAN_GENUCHTEN_HPP
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#include "ThreePhaseParkerVanGenuchtenParams.hpp"
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#include <algorithm>
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namespace Opm {
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/*!
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* \ingroup FluidMatrixInteractions
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*
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* \brief Implementation of three-phase capillary pressure and
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* relative permeability relations proposed by Parker and van
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* Genuchten.
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*
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* Reference: J.B. Kool, J.C. Parker, M.Th. van Genuchten: Parameter
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* Estimation for Unsaturated Flow and Transport Models -- A Review;
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* Journal of Hydrology, 91 (1987) 255-293
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*/
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template <class TraitsT,
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class ParamsT = ThreePhaseParkerVanGenuchtenParams<TraitsT> >
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class ThreePhaseParkerVanGenuchten
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{
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public:
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static_assert(TraitsT::numPhases == 3,
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"The number of phases considered by this capillary pressure "
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"law is always three!");
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typedef TraitsT Traits;
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typedef ParamsT Params;
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typedef typename Traits::Scalar Scalar;
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static const int numPhases = 3;
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static const int wPhaseIdx = Traits::wPhaseIdx;
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static const int nPhaseIdx = Traits::nPhaseIdx;
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static const int gPhaseIdx = Traits::gPhaseIdx;
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//! Specify whether this material law implements the two-phase
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//! convenience API
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static const bool implementsTwoPhaseApi = false;
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//! Specify whether this material law implements the two-phase
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//! convenience API which only depends on the phase saturations
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static const bool implementsTwoPhaseSatApi = false;
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//! Specify whether the quantities defined by this material law
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//! are saturation dependent
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static const bool isSaturationDependent = true;
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//! Specify whether the quantities defined by this material law
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//! are dependent on the absolute pressure
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static const bool isPressureDependent = false;
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//! Specify whether the quantities defined by this material law
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//! are temperature dependent
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static const bool isTemperatureDependent = false;
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//! Specify whether the quantities defined by this material law
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//! are dependent on the phase composition
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static const bool isCompositionDependent = false;
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/*!
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* \brief Implements the three phase capillary pressure law
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* proposed by Parker and van Genuchten.
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*
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* This material law is valid for three fluid phases and only
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* depends on the saturations.
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*
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* \param values Container for the return values
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* \param params Parameters
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* \param state The fluid state
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*/
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template <class ContainerT, class FluidState>
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static void capillaryPressures(ContainerT &values,
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const Params ¶ms,
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const FluidState &fluidState)
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{
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values[gPhaseIdx] = pcgn(params, fluidState);
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values[nPhaseIdx] = 0;
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values[wPhaseIdx] = - pcnw(params, fluidState);
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}
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/*!
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* \brief Capillary pressure between the gas and the non-wetting
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* liquid (i.e., oil) phase.
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*
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* This is defined as
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* \f[
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* p_{c,gn} = p_g - p_n
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* \f]
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*/
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template <class FluidState>
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static Scalar pcgn(const Params ¶ms,
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const FluidState &fluidState)
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{
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Scalar PC_VG_REG = 0.01;
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// sum of liquid saturations
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Scalar St =
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fluidState.saturation(wPhaseIdx)
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+ fluidState.saturation(nPhaseIdx);
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Scalar Se = (St - params.Swrx())/(1. - params.Swrx());
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// regularization
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if (Se < 0.0)
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Se=0.0;
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if (Se > 1.0)
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Se=1.0;
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if (Se>PC_VG_REG && Se<1-PC_VG_REG)
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{
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Scalar x = std::pow(Se,-1/params.vgM()) - 1;
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return std::pow(x, 1 - params.vgM())/params.vgAlpha();
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}
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// value and derivative at regularization point
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Scalar Se_regu;
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if (Se<=PC_VG_REG)
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Se_regu = PC_VG_REG;
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else
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Se_regu = 1-PC_VG_REG;
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Scalar x = std::pow(Se_regu,-1/params.vgM())-1;
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Scalar pc = std::pow(x, 1/params.vgN())/params.vgAlpha();
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Scalar pc_prime =
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std::pow(x, 1/params.vgN()-1)
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* std::pow(Se_regu,-1/params.vgM()-1)
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/ (-params.vgM())
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/ params.vgAlpha()
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/ (1 - params.Sgr() - params.Swrx())
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/ params.vgN();
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// evaluate tangential
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return ((Se-Se_regu)*pc_prime + pc)/params.betaGN();
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}
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/*!
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* \brief Capillary pressure between the non-wetting liquid (i.e.,
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* oil) and the wetting liquid (i.e., water) phase.
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*
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* This is defined as
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* \f[
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* p_{c,nw} = p_n - p_w
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* \f]
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*/
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template <class FluidState>
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static Scalar pcnw(const Params ¶ms,
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const FluidState &fluidState)
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{
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Scalar Sw = fluidState.saturation(wPhaseIdx);
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Scalar Se = (Sw-params.Swr())/(1.-params.Snr());
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Scalar PC_VG_REG = 0.01;
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// regularization
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if (Se<0.0)
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Se=0.0;
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if (Se>1.0)
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Se=1.0;
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if (Se>PC_VG_REG && Se<1-PC_VG_REG) {
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Scalar x = std::pow(Se,-1/params.vgM()) - 1.0;
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x = std::pow(x, 1 - params.vgM());
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return x/params.vgAlpha();
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}
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// value and derivative at regularization point
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Scalar Se_regu;
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if (Se<=PC_VG_REG)
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Se_regu = PC_VG_REG;
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else
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Se_regu = 1.0 - PC_VG_REG;
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Scalar x = std::pow(Se_regu,-1/params.vgM())-1;
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Scalar pc = std::pow(x, 1/params.vgN())/params.vgAlpha();
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Scalar pc_prime =
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std::pow(x,1/params.vgN()-1)
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* std::pow(Se_regu, -1.0/params.vgM() - 1)
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/ (-params.vgM())
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/ params.vgAlpha()
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/ (1-params.Snr()-params.Swr())
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/ params.vgN();
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// evaluate tangential
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return ((Se-Se_regu)*pc_prime + pc)/params.betaNW();
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}
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/*!
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* \brief The saturation-capillary pressure curve.
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*
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*/
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template <class ContainerT, class FluidState>
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static void saturations(ContainerT &values,
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const Params ¶ms,
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const FluidState &fluidState)
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{ OPM_THROW(std::logic_error, "Not implemented: inverse capillary pressures"); }
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/*!
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* \brief The saturation of the gas phase.
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*/
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template <class FluidState>
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static Scalar Sg(const Params ¶ms,
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const FluidState &fluidState)
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{ OPM_THROW(std::logic_error, "Not implemented: Sg()"); }
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/*!
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* \brief The saturation of the non-wetting (i.e., oil) phase.
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*/
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template <class FluidState>
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static Scalar Sn(const Params ¶ms,
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const FluidState &fluidState)
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{ OPM_THROW(std::logic_error, "Not implemented: Sn()"); }
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/*!
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* \brief The saturation of the wetting (i.e., water) phase.
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*/
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template <class FluidState>
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static Scalar Sw(const Params ¶ms,
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const FluidState &fluidState)
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{ OPM_THROW(std::logic_error, "Not implemented: Sw()"); }
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/*!
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* \brief The relative permeability of all phases.
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*/
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template <class ContainerT, class FluidState>
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static void relativePermeabilities(ContainerT &values,
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const Params ¶ms,
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const FluidState &fluidState)
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{
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values[wPhaseIdx] = krw(params, fluidState);
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values[nPhaseIdx] = krn(params, fluidState);
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values[gPhaseIdx] = krg(params, fluidState);
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}
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/*!
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* \brief The relative permeability for the wetting phase of the
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* medium implied by van Genuchten's parameterization.
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*
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* The permeability of water in a 3p system equals the standard 2p description.
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* (see p61. in "Comparison of the Three-Phase Oil Relative Permeability Models"
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* MOJDEH DELSHAD and GARY A. POPE, Transport in Porous Media 4 (1989), 59-83.)
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*/
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template <class FluidState>
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static Scalar krw(const Params ¶ms,
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const FluidState &fluidState)
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{
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// transformation to effective saturation
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Scalar Se = (fluidState.saturation(wPhaseIdx) - params.Swr()) / (1-params.Swr());
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// regularization
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if(Se > 1.0) return 1.;
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if(Se < 0.0) return 0.;
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Scalar r = 1. - std::pow(1 - std::pow(Se, 1/params.vgM()), params.vgM());
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return std::sqrt(Se)*r*r;
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}
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/*!
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* \brief The relative permeability for the non-wetting phase
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* due to the model of Parker et al. (1987).
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*
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* See model 7 of "Comparison of the Three-Phase Oil Relative
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* Permeability Models" M. Delshad and G. A. Pope, Transport in
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* Porous Media 4 (1989), 59-83; or -- more comprehensively --
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* "Estimation of primary drainage three-phase relative
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* permeability for organic liquid transport in the vadose zone",
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* L. I. Oliveira, A. H. Demond, Journal of Contaminant Hydrology
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* 66 (2003), 261-285
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*/
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template <class FluidState>
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static Scalar krn(const Params ¶ms,
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const FluidState &fluidState)
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{
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Scalar Sn = fluidState.saturation(nPhaseIdx);
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Scalar Sw = fluidState.saturation(wPhaseIdx);
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Scalar Swe = std::min((Sw - params.Swr()) / (1 - params.Swr()), 1.);
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Scalar Ste = std::min((Sw + Sn - params.Swr()) / (1 - params.Swr()), 1.);
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// regularization
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if(Swe <= 0.0) Swe = 0.;
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if(Ste <= 0.0) Ste = 0.;
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if(Ste - Swe <= 0.0) return 0.;
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Scalar krn_;
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krn_ = std::pow(1 - std::pow(Swe, 1/params.vgM()), params.vgM());
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krn_ -= std::pow(1 - std::pow(Ste, 1/params.vgM()), params.vgM());
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krn_ *= krn_;
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if (params.krRegardsSnr())
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{
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// regard Snr in the permeability of the non-wetting
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// phase, see Helmig1997
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Scalar resIncluded =
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std::max(std::min(Sw - params.Snr() / (1-params.Swr()), 1.0),
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0.0);
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krn_ *= std::sqrt(resIncluded );
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}
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else
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krn_ *= std::sqrt(Sn / (1 - params.Swr()));
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return krn_;
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}
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/*!
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* \brief The relative permeability for the non-wetting phase
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* of the medium implied by van Genuchten's
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* parameterization.
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*
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* The permeability of gas in a three-phase system equals the
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* standard two-phase description. (see p61. of "Comparison of the
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* Three-Phase Oil Relative Permeability Models" M. Delshad and
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* G. A. Pope, Transport in Porous Media 4 (1989), 59-83.)
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*/
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template <class FluidState>
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static Scalar krg(const Params ¶ms,
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const FluidState &fluidState)
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{
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Scalar Sg = fluidState.saturation(gPhaseIdx);
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Scalar Se = std::min(((1-Sg) - params.Sgr()) / (1 - params.Sgr()), 1.);
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// regularization
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if(Se > 1.0)
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return 0.0;
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if(Se < 0.0)
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return 1.0;
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Scalar scaleFactor = 1.;
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if (Sg<=0.1) {
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scaleFactor = (Sg - params.Sgr())/(0.1 - params.Sgr());
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if (scaleFactor < 0.)
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scaleFactor = 0.;
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}
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return scaleFactor
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* std::pow(1 - Se, 1.0/3.)
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* std::pow(1 - std::pow(Se, 1/params.vgM()), 2*params.vgM());
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}
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/*!
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* \brief The derivative of all capillary pressures in regard to
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* a given phase saturation.
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*/
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template <class ContainerT, class FluidState>
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static void dCapillaryPressures_dSaturation(ContainerT &values,
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const Params ¶ms,
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const FluidState &state,
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int satPhaseIdx)
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{
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OPM_THROW(std::logic_error,
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"Not implemented: dCapillaryPressures_dSaturation()");
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}
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/*!
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* \brief The derivative of all capillary pressures in regard to
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* a given phase pressure.
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*/
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template <class ContainerT, class FluidState>
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static void dCapillaryPressures_dPressure(ContainerT &values,
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const Params ¶ms,
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const FluidState &state,
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int pPhaseIdx)
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{
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// -> not pressure dependent
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for (int pcPhaseIdx = 0; pcPhaseIdx < numPhases; ++pcPhaseIdx)
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values[pcPhaseIdx] = 0.0;
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}
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/*!
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* \brief The derivative of all capillary pressures in regard to
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* temperature.
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*/
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template <class ContainerT, class FluidState>
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static void dCapillaryPressures_dTemperature(ContainerT &values,
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const Params ¶ms,
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const FluidState &state)
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{
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// -> not temperature dependent
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for (int pcPhaseIdx = 0; pcPhaseIdx < numPhases; ++pcPhaseIdx)
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values[pcPhaseIdx] = 0.0;
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}
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/*!
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* \brief The derivative of all capillary pressures in regard to
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* a given mole fraction of a component in a phase.
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*/
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template <class ContainerT, class FluidState>
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static void dCapillaryPressures_dMoleFraction(ContainerT &values,
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const Params ¶ms,
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const FluidState &state,
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int phaseIdx,
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int compIdx)
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{
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// -> not composition dependent
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for (int pcPhaseIdx = 0; pcPhaseIdx < numPhases; ++pcPhaseIdx)
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values[pcPhaseIdx] = 0.0;
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}
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/*!
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* \brief The derivative of all relative permeabilities in regard to
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* a given phase saturation.
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*/
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template <class ContainerT, class FluidState>
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static void dRelativePermeabilities_dSaturation(ContainerT &values,
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const Params ¶ms,
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const FluidState &state,
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int satPhaseIdx)
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{
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OPM_THROW(std::logic_error,
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"Not implemented: dRelativePermeabilities_dSaturation()");
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}
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/*!
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* \brief The derivative of all relative permeabilities in regard to
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* a given phase pressure.
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*/
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template <class ContainerT, class FluidState>
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static void dRelativePermeabilities_dPressure(ContainerT &values,
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const Params ¶ms,
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const FluidState &state,
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int pPhaseIdx)
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{
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// -> not pressure dependent
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for (int krPhaseIdx = 0; krPhaseIdx < numPhases; ++krPhaseIdx)
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values[krPhaseIdx] = 0.0;
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}
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/*!
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* \brief The derivative of all relative permeabilities in regard to
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* temperature.
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*/
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template <class ContainerT, class FluidState>
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static void dRelativePermeabilities_dTemperature(ContainerT &values,
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const Params ¶ms,
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const FluidState &state)
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{
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// -> not temperature dependent
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for (int krPhaseIdx = 0; krPhaseIdx < numPhases; ++krPhaseIdx)
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values[krPhaseIdx] = 0.0;
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}
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/*!
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* \brief The derivative of all relative permeabilities in regard to
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* a given mole fraction of a component in a phase.
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*/
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template <class ContainerT, class FluidState>
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static void dRelativePermeabilities_dMoleFraction(ContainerT &values,
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const Params ¶ms,
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const FluidState &state,
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int phaseIdx,
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int compIdx)
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{
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// -> not composition dependent
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for (int krPhaseIdx = 0; krPhaseIdx < numPhases; ++krPhaseIdx)
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values[krPhaseIdx] = 0.0;
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}
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};
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} // namespace Opm
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#endif
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