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| 1 | // -*- mode: C++; tab-width: 4; indent-tabs-mode: nil; c-basic-offset: 4 -*- | ||
| 2 | // vi: set et ts=4 sw=4 sts=4: | ||
| 3 | // | ||
| 4 | // SPDX-FileCopyrightInfo: Copyright © DuMux Project contributors, see AUTHORS.md in root folder | ||
| 5 | // SPDX-License-Identifier: GPL-3.0-or-later | ||
| 6 | // | ||
| 7 | /*! | ||
| 8 | * \file | ||
| 9 | * \ingroup TwoPNCModel | ||
| 10 | * \brief Contains the quantities which are constant within a | ||
| 11 | * finite volume in the two-phase, n-component model. | ||
| 12 | */ | ||
| 13 | |||
| 14 | #ifndef DUMUX_2PNC_VOLUME_VARIABLES_HH | ||
| 15 | #define DUMUX_2PNC_VOLUME_VARIABLES_HH | ||
| 16 | |||
| 17 | #include <iostream> | ||
| 18 | #include <vector> | ||
| 19 | |||
| 20 | #include <dumux/common/math.hh> | ||
| 21 | #include <dumux/discretization/method.hh> | ||
| 22 | |||
| 23 | #include <dumux/porousmediumflow/volumevariables.hh> | ||
| 24 | #include <dumux/porousmediumflow/nonisothermal/volumevariables.hh> | ||
| 25 | |||
| 26 | #include <dumux/material/fluidstates/compositional.hh> | ||
| 27 | #include <dumux/material/solidstates/updatesolidvolumefractions.hh> | ||
| 28 | #include <dumux/material/constraintsolvers/computefromreferencephase.hh> | ||
| 29 | #include <dumux/material/constraintsolvers/misciblemultiphasecomposition.hh> | ||
| 30 | |||
| 31 | #include <dumux/porousmediumflow/2p/formulation.hh> | ||
| 32 | |||
| 33 | #include "primaryvariableswitch.hh" | ||
| 34 | |||
| 35 | namespace Dumux { | ||
| 36 | |||
| 37 | /*! | ||
| 38 | * \ingroup TwoPNCModel | ||
| 39 | * \brief Contains the quantities which are are constant within a | ||
| 40 | * finite volume in the two-phase, n-component model. | ||
| 41 | */ | ||
| 42 | template <class Traits> | ||
| 43 | 828574 | class TwoPNCVolumeVariables | |
| 44 | : public PorousMediumFlowVolumeVariables<Traits> | ||
| 45 | , public EnergyVolumeVariables<Traits, TwoPNCVolumeVariables<Traits> > | ||
| 46 | { | ||
| 47 | using ParentType = PorousMediumFlowVolumeVariables<Traits>; | ||
| 48 | using EnergyVolVars = EnergyVolumeVariables<Traits, TwoPNCVolumeVariables<Traits> >; | ||
| 49 | using Scalar = typename Traits::PrimaryVariables::value_type; | ||
| 50 | using PermeabilityType = typename Traits::PermeabilityType; | ||
| 51 | using FS = typename Traits::FluidSystem; | ||
| 52 | using ModelTraits = typename Traits::ModelTraits; | ||
| 53 | static constexpr int numFluidComps = ParentType::numFluidComponents(); | ||
| 54 | enum | ||
| 55 | { | ||
| 56 | numMajorComponents = ModelTraits::numFluidPhases(), | ||
| 57 | |||
| 58 | // phase indices | ||
| 59 | phase0Idx = FS::phase0Idx, | ||
| 60 | phase1Idx = FS::phase1Idx, | ||
| 61 | |||
| 62 | // component indices | ||
| 63 | comp0Idx = FS::comp0Idx, | ||
| 64 | comp1Idx = FS::comp1Idx, | ||
| 65 | |||
| 66 | // phase presence enums | ||
| 67 | secondPhaseOnly = ModelTraits::Indices::secondPhaseOnly, | ||
| 68 | firstPhaseOnly = ModelTraits::Indices::firstPhaseOnly, | ||
| 69 | bothPhases = ModelTraits::Indices::bothPhases, | ||
| 70 | |||
| 71 | // primary variable indices | ||
| 72 | pressureIdx = ModelTraits::Indices::pressureIdx, | ||
| 73 | switchIdx = ModelTraits::Indices::switchIdx | ||
| 74 | }; | ||
| 75 | |||
| 76 | static constexpr auto formulation = ModelTraits::priVarFormulation(); | ||
| 77 | static constexpr bool setFirstPhaseMoleFractions = ModelTraits::setMoleFractionsForFirstPhase(); | ||
| 78 | |||
| 79 | using MiscibleMultiPhaseComposition = Dumux::MiscibleMultiPhaseComposition<Scalar, FS>; | ||
| 80 | using ComputeFromReferencePhase = Dumux::ComputeFromReferencePhase<Scalar, FS>; | ||
| 81 | using EffDiffModel = typename Traits::EffectiveDiffusivityModel; | ||
| 82 | using DiffusionCoefficients = typename Traits::DiffusionType::DiffusionCoefficientsContainer; | ||
| 83 | |||
| 84 | public: | ||
| 85 | //! Export fluid state type | ||
| 86 | using FluidState = typename Traits::FluidState; | ||
| 87 | //! Export fluid system type | ||
| 88 | using FluidSystem = typename Traits::FluidSystem; | ||
| 89 | //! Export the indices | ||
| 90 | using Indices = typename ModelTraits::Indices; | ||
| 91 | //! Export type of solid state | ||
| 92 | using SolidState = typename Traits::SolidState; | ||
| 93 | //! Export type of solid system | ||
| 94 | using SolidSystem = typename Traits::SolidSystem; | ||
| 95 | //! Export the primary variable switch | ||
| 96 | using PrimaryVariableSwitch = TwoPNCPrimaryVariableSwitch; | ||
| 97 | |||
| 98 | //! Return whether moles or masses are balanced | ||
| 99 | static constexpr bool useMoles() { return Traits::ModelTraits::useMoles(); } | ||
| 100 | //! Return the two-phase formulation used here | ||
| 101 | static constexpr TwoPFormulation priVarFormulation() { return formulation; } | ||
| 102 | |||
| 103 | // check for permissive specifications | ||
| 104 | static_assert(useMoles(), "use moles has to be set true in the 2pnc model"); | ||
| 105 | static_assert(ModelTraits::numFluidPhases() == 2, "NumPhases set in the model is not two!"); | ||
| 106 | static_assert((formulation == TwoPFormulation::p0s1 || formulation == TwoPFormulation::p1s0), "Chosen TwoPFormulation not supported!"); | ||
| 107 | |||
| 108 | /*! | ||
| 109 | * \brief Updates all quantities for a given control volume. | ||
| 110 | * | ||
| 111 | * \param elemSol A vector containing all primary variables connected to the element | ||
| 112 | * \param problem The object specifying the problem which ought to | ||
| 113 | * be simulated | ||
| 114 | * \param element An element which contains part of the control volume | ||
| 115 | * \param scv The sub control volume | ||
| 116 | */ | ||
| 117 | template<class ElemSol, class Problem, class Element, class Scv> | ||
| 118 | 14710884 | void update(const ElemSol &elemSol, | |
| 119 | const Problem &problem, | ||
| 120 | const Element &element, | ||
| 121 | const Scv& scv) | ||
| 122 | { | ||
| 123 | 14710884 | ParentType::update(elemSol, problem, element, scv); | |
| 124 | |||
| 125 | 14710884 | completeFluidState(elemSol, problem, element, scv, fluidState_, solidState_); | |
| 126 | |||
| 127 | ///////////// | ||
| 128 | // calculate the remaining quantities | ||
| 129 | ///////////// | ||
| 130 | |||
| 131 | 14710884 | const auto& spatialParams = problem.spatialParams(); | |
| 132 | 14710897 | const auto fluidMatrixInteraction = spatialParams.fluidMatrixInteraction(element, scv, elemSol); | |
| 133 | |||
| 134 | 14710884 | const int wPhaseIdx = fluidState_.wettingPhase(); | |
| 135 | 14710884 | const int nPhaseIdx = 1 - wPhaseIdx; | |
| 136 | |||
| 137 | // mobilities -> require wetting phase saturation as parameter! | ||
| 138 |
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32849368 | mobility_[wPhaseIdx] = fluidMatrixInteraction.krw(saturation(wPhaseIdx))/fluidState_.viscosity(wPhaseIdx); |
| 139 |
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32849368 | mobility_[nPhaseIdx] = fluidMatrixInteraction.krn(saturation(wPhaseIdx))/fluidState_.viscosity(nPhaseIdx); |
| 140 | |||
| 141 | //update porosity before calculating the effective properties depending on it | ||
| 142 |
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14710884 | updateSolidVolumeFractions(elemSol, problem, element, scv, solidState_, numFluidComps); |
| 143 | |||
| 144 | 14710884 | auto getEffectiveDiffusionCoefficient = [&](int phaseIdx, int compIIdx, int compJIdx) | |
| 145 | { | ||
| 146 | 89111480 | return EffDiffModel::effectiveDiffusionCoefficient(*this, phaseIdx, compIIdx, compJIdx); | |
| 147 | }; | ||
| 148 | |||
| 149 |
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14710884 | effectiveDiffCoeff_.update(getEffectiveDiffusionCoefficient); |
| 150 | |||
| 151 | // calculate the remaining quantities | ||
| 152 |
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14710884 | EnergyVolVars::updateSolidEnergyParams(elemSol, problem, element, scv, solidState_); |
| 153 |
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24341435 | permeability_ = spatialParams.permeability(element, scv, elemSol); |
| 154 |
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14710884 | EnergyVolVars::updateEffectiveThermalConductivity(); |
| 155 | 14710871 | } | |
| 156 | |||
| 157 | /*! | ||
| 158 | * \brief Sets complete fluid state. | ||
| 159 | * | ||
| 160 | * \param elemSol A vector containing all primary variables connected to the element | ||
| 161 | * \param problem The object specifying the problem which ought to be simulated | ||
| 162 | * \param element An element which contains part of the control volume | ||
| 163 | * \param scv The sub-control volume | ||
| 164 | * \param fluidState A container with the current (physical) state of the fluid | ||
| 165 | * \param solidState A container with the current (physical) state of the solid | ||
| 166 | * | ||
| 167 | * Set temperature, saturations, capillary pressures, viscosities, densities and enthalpies. | ||
| 168 | */ | ||
| 169 | template<class ElemSol, class Problem, class Element, class Scv> | ||
| 170 | 14710884 | void completeFluidState(const ElemSol& elemSol, | |
| 171 | const Problem& problem, | ||
| 172 | const Element& element, | ||
| 173 | const Scv& scv, | ||
| 174 | FluidState& fluidState, | ||
| 175 | SolidState& solidState) | ||
| 176 | { | ||
| 177 | 14710884 | EnergyVolVars::updateTemperature(elemSol, problem, element, scv, fluidState, solidState); | |
| 178 | |||
| 179 | 14710884 | const auto& priVars = elemSol[scv.localDofIndex()]; | |
| 180 | 14710884 | const auto phasePresence = priVars.state(); | |
| 181 | |||
| 182 |
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14710884 | const auto& spatialParams = problem.spatialParams(); |
| 183 |
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14752544 | const auto fluidMatrixInteraction = spatialParams.fluidMatrixInteraction(element, scv, elemSol); |
| 184 |
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14710884 | const auto wPhaseIdx = spatialParams.template wettingPhase<FluidSystem>(element, scv, elemSol); |
| 185 |
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14710884 | fluidState.setWettingPhase(wPhaseIdx); |
| 186 | |||
| 187 | // set the saturations | ||
| 188 |
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14710884 | if (phasePresence == secondPhaseOnly) |
| 189 | { | ||
| 190 | 2401 | fluidState.setSaturation(phase0Idx, 0.0); | |
| 191 | 2401 | fluidState.setSaturation(phase1Idx, 1.0); | |
| 192 | } | ||
| 193 |
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14708483 | else if (phasePresence == firstPhaseOnly) |
| 194 | { | ||
| 195 | 3444959 | fluidState.setSaturation(phase0Idx, 1.0); | |
| 196 | 3444959 | fluidState.setSaturation(phase1Idx, 0.0); | |
| 197 | } | ||
| 198 |
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11263524 | else if (phasePresence == bothPhases) |
| 199 | { | ||
| 200 | if (formulation == TwoPFormulation::p0s1) | ||
| 201 | { | ||
| 202 | 18394106 | fluidState.setSaturation(phase1Idx, priVars[switchIdx]); | |
| 203 | 18394106 | fluidState.setSaturation(phase0Idx, 1 - priVars[switchIdx]); | |
| 204 | } | ||
| 205 | else | ||
| 206 | { | ||
| 207 | 4132942 | fluidState.setSaturation(phase0Idx, priVars[switchIdx]); | |
| 208 | 4132942 | fluidState.setSaturation(phase1Idx, 1 - priVars[switchIdx]); | |
| 209 | } | ||
| 210 | } | ||
| 211 | else | ||
| 212 | ✗ | DUNE_THROW(Dune::InvalidStateException, "phasePresence: " << phasePresence << " is invalid."); | |
| 213 | |||
| 214 | // set pressures of the fluid phases | ||
| 215 |
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20352526 | pc_ = fluidMatrixInteraction.pc(fluidState.saturation(wPhaseIdx)); |
| 216 | if (formulation == TwoPFormulation::p0s1) | ||
| 217 | { | ||
| 218 |
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24383980 | fluidState.setPressure(phase0Idx, priVars[pressureIdx]); |
| 219 |
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24383980 | fluidState.setPressure(phase1Idx, (wPhaseIdx == phase0Idx) ? priVars[pressureIdx] + pc_ |
| 220 | : priVars[pressureIdx] - pc_); | ||
| 221 | } | ||
| 222 | else | ||
| 223 | { | ||
| 224 |
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5037788 | fluidState.setPressure(phase1Idx, priVars[pressureIdx]); |
| 225 |
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5037788 | fluidState.setPressure(phase0Idx, (wPhaseIdx == phase0Idx) ? priVars[pressureIdx] - pc_ |
| 226 |
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603426 | : priVars[pressureIdx] + pc_); |
| 227 | } | ||
| 228 | |||
| 229 | // calculate the phase compositions | ||
| 230 | typename FluidSystem::ParameterCache paramCache; | ||
| 231 | |||
| 232 | // now comes the tricky part: calculate phase composition | ||
| 233 |
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14710884 | if (phasePresence == bothPhases) |
| 234 | { | ||
| 235 | // both phases are present, phase composition results from | ||
| 236 | // the first <-> second phase equilibrium. This is the job | ||
| 237 | // of the "MiscibleMultiPhaseComposition" constraint solver | ||
| 238 | |||
| 239 | // set the known mole fractions in the fluidState so that they | ||
| 240 | // can be used by the MiscibleMultiPhaseComposition constraint solver | ||
| 241 | |||
| 242 | 41495 | const int knownPhaseIdx = setFirstPhaseMoleFractions ? phase0Idx : phase1Idx; | |
| 243 |
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22485553 | for (int compIdx = numMajorComponents; compIdx < ModelTraits::numFluidComponents(); ++compIdx) |
| 244 | 22444058 | fluidState.setMoleFraction(knownPhaseIdx, compIdx, priVars[compIdx]); | |
| 245 | |||
| 246 |
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11263524 | MiscibleMultiPhaseComposition::solve(fluidState, |
| 247 | paramCache, | ||
| 248 | knownPhaseIdx); | ||
| 249 | } | ||
| 250 |
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3447360 | else if (phasePresence == secondPhaseOnly) |
| 251 | { | ||
| 252 | ✗ | Dune::FieldVector<Scalar, ModelTraits::numFluidComponents()> moleFrac; | |
| 253 | |||
| 254 | 4802 | moleFrac[comp0Idx] = priVars[switchIdx]; | |
| 255 | 2401 | Scalar sumMoleFracOtherComponents = moleFrac[comp0Idx]; | |
| 256 | |||
| 257 |
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2401 | for (int compIdx = numMajorComponents; compIdx < ModelTraits::numFluidComponents(); ++compIdx) |
| 258 | { | ||
| 259 | ✗ | moleFrac[compIdx] = priVars[compIdx]; | |
| 260 | ✗ | sumMoleFracOtherComponents += moleFrac[compIdx]; | |
| 261 | } | ||
| 262 | |||
| 263 | 2401 | moleFrac[comp1Idx] = 1 - sumMoleFracOtherComponents; | |
| 264 | |||
| 265 | // Set fluid state mole fractions | ||
| 266 |
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7203 | for (int compIdx = 0; compIdx < ModelTraits::numFluidComponents(); ++compIdx) |
| 267 |
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9604 | fluidState.setMoleFraction(phase1Idx, compIdx, moleFrac[compIdx]); |
| 268 | |||
| 269 | // calculate the composition of the remaining phases (as | ||
| 270 | // well as the densities of all phases). this is the job | ||
| 271 | // of the "ComputeFromReferencePhase" constraint solver | ||
| 272 |
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2401 | ComputeFromReferencePhase::solve(fluidState, |
| 273 | paramCache, | ||
| 274 | phase1Idx); | ||
| 275 | } | ||
| 276 |
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3444959 | else if (phasePresence == firstPhaseOnly) |
| 277 | { | ||
| 278 | // only the first phase is present, i.e. first phase composition | ||
| 279 | // is stored explicitly. extract _mass_ fractions in the second phase | ||
| 280 | 3048195 | Dune::FieldVector<Scalar, ModelTraits::numFluidComponents()> moleFrac; | |
| 281 | |||
| 282 | 6889918 | moleFrac[comp1Idx] = priVars[switchIdx]; | |
| 283 | 3444959 | Scalar sumMoleFracOtherComponents = moleFrac[comp1Idx]; | |
| 284 |
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22067786 | for (int compIdx = numMajorComponents; compIdx < ModelTraits::numFluidComponents(); ++compIdx) |
| 285 | { | ||
| 286 | 37245654 | moleFrac[compIdx] = priVars[compIdx]; | |
| 287 | |||
| 288 | 37245654 | sumMoleFracOtherComponents += moleFrac[compIdx]; | |
| 289 | } | ||
| 290 | |||
| 291 | 3444959 | moleFrac[comp0Idx] = 1 - sumMoleFracOtherComponents; | |
| 292 | |||
| 293 | // convert mass to mole fractions and set the fluid state | ||
| 294 |
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28957704 | for (int compIdx = 0; compIdx < ModelTraits::numFluidComponents(); ++compIdx) |
| 295 |
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51809386 | fluidState.setMoleFraction(phase0Idx, compIdx, moleFrac[compIdx]); |
| 296 | |||
| 297 | // calculate the composition of the remaining phases (as | ||
| 298 | // well as the densities of all phases). this is the job | ||
| 299 | // of the "ComputeFromReferencePhase" constraint solver | ||
| 300 |
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3444959 | ComputeFromReferencePhase::solve(fluidState, |
| 301 | paramCache, | ||
| 302 | phase0Idx); | ||
| 303 | } | ||
| 304 | paramCache.updateAll(fluidState); | ||
| 305 |
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44132652 | for (int phaseIdx = 0; phaseIdx < ModelTraits::numFluidPhases(); ++phaseIdx) |
| 306 | { | ||
| 307 |
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29421768 | Scalar mu = FluidSystem::viscosity(fluidState, paramCache, phaseIdx); |
| 308 |
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29421768 | Scalar h = EnergyVolVars::enthalpy(fluidState, paramCache, phaseIdx); |
| 309 | 29421768 | fluidState.setViscosity(phaseIdx, mu); | |
| 310 | 58843536 | fluidState.setEnthalpy(phaseIdx, h); | |
| 311 | } | ||
| 312 | 14710884 | } | |
| 313 | |||
| 314 | /*! | ||
| 315 | * \brief Returns the phase state for the control-volume. | ||
| 316 | */ | ||
| 317 | const FluidState &fluidState() const | ||
| 318 | 4808980 | { return fluidState_; } | |
| 319 | |||
| 320 | /*! | ||
| 321 | * \brief Returns the phase state for the control-volume. | ||
| 322 | */ | ||
| 323 | const SolidState &solidState() const | ||
| 324 | 874461 | { return solidState_; } | |
| 325 | |||
| 326 | /*! | ||
| 327 | * \brief Returns the average molar mass \f$\mathrm{[kg/mol]}\f$ of the fluid phase. | ||
| 328 | * | ||
| 329 | * \param phaseIdx The phase index | ||
| 330 | */ | ||
| 331 | Scalar averageMolarMass(int phaseIdx) const | ||
| 332 | 1718244 | { return fluidState_.averageMolarMass(phaseIdx); } | |
| 333 | |||
| 334 | /*! | ||
| 335 | * \brief Returns the saturation of a given phase within | ||
| 336 | * the control volume in \f$[-]\f$. | ||
| 337 | * | ||
| 338 | * \param phaseIdx The phase index | ||
| 339 | */ | ||
| 340 | Scalar saturation(int phaseIdx) const | ||
| 341 |
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782714516 | { return fluidState_.saturation(phaseIdx); } |
| 342 | |||
| 343 | /*! | ||
| 344 | * \brief Returns the mass density of a given phase within the | ||
| 345 | * control volume. | ||
| 346 | * | ||
| 347 | * \param phaseIdx The phase index | ||
| 348 | */ | ||
| 349 | Scalar density(int phaseIdx) const | ||
| 350 | 287126400 | { return fluidState_.density(phaseIdx); } | |
| 351 | |||
| 352 | /*! | ||
| 353 | * \brief Returns the dynamic viscosity of a given phase within the | ||
| 354 | * control volume. | ||
| 355 | * | ||
| 356 | * \param phaseIdx The phase index | ||
| 357 | */ | ||
| 358 | Scalar viscosity(int phaseIdx) const | ||
| 359 | { return fluidState_.viscosity(phaseIdx); } | ||
| 360 | |||
| 361 | /*! | ||
| 362 | * \brief Returns the molar density of a given phase within the | ||
| 363 | * control volume. | ||
| 364 | * | ||
| 365 | * \param phaseIdx The phase index | ||
| 366 | */ | ||
| 367 | 511374288 | Scalar molarDensity(int phaseIdx) const | |
| 368 | { | ||
| 369 |
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511374288 | if (phaseIdx < ModelTraits::numFluidPhases()) |
| 370 |
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1055548340 | return fluidState_.molarDensity(phaseIdx); |
| 371 | |||
| 372 | else | ||
| 373 | ✗ | DUNE_THROW(Dune::InvalidStateException, "Invalid phase index " << phaseIdx); | |
| 374 | } | ||
| 375 | |||
| 376 | /*! | ||
| 377 | * \brief Returns the effective pressure of a given phase within | ||
| 378 | * the control volume. | ||
| 379 | * | ||
| 380 | * \param phaseIdx The phase index | ||
| 381 | */ | ||
| 382 | Scalar pressure(int phaseIdx) const | ||
| 383 |
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142121536 | { return fluidState_.pressure(phaseIdx); } |
| 384 | |||
| 385 | /*! | ||
| 386 | * \brief Returns temperature inside the sub-control volume. | ||
| 387 | * | ||
| 388 | * Note that we assume thermodynamic equilibrium, i.e. the | ||
| 389 | * temperature of the rock matrix and of all fluid phases are | ||
| 390 | * identical. | ||
| 391 | */ | ||
| 392 | Scalar temperature() const | ||
| 393 |
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4656282 | { return fluidState_.temperature(/*phaseIdx=*/0); } |
| 394 | |||
| 395 | /*! | ||
| 396 | * \brief Returns the effective mobility of a given phase within | ||
| 397 | * the control volume. | ||
| 398 | * | ||
| 399 | * \param phaseIdx The phase index | ||
| 400 | */ | ||
| 401 | Scalar mobility(int phaseIdx) const | ||
| 402 | 104826148 | { return mobility_[phaseIdx]; } | |
| 403 | |||
| 404 | /*! | ||
| 405 | * \brief Returns the effective capillary pressure within the control volume | ||
| 406 | * in \f$[kg/(m*s^2)=N/m^2=Pa]\f$. | ||
| 407 | */ | ||
| 408 | ✗ | Scalar capillaryPressure() const | |
| 409 | ✗ | { return pc_; } | |
| 410 | |||
| 411 | /*! | ||
| 412 | * \brief Returns the average porosity within the control volume. | ||
| 413 | */ | ||
| 414 | Scalar porosity() const | ||
| 415 |
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476730062 | { return solidState_.porosity(); } |
| 416 | |||
| 417 | /*! | ||
| 418 | * \brief Returns the permeability within the control volume. | ||
| 419 | */ | ||
| 420 | const PermeabilityType& permeability() const | ||
| 421 | 1925436 | { return permeability_; } | |
| 422 | |||
| 423 | /*! | ||
| 424 | * \brief Returns the binary diffusion coefficients for a phase in \f$[m^2/s]\f$. | ||
| 425 | */ | ||
| 426 | ✗ | Scalar diffusionCoefficient(int phaseIdx, int compIIdx, int compJIdx) const | |
| 427 | { | ||
| 428 | typename FluidSystem::ParameterCache paramCache; | ||
| 429 | 52921044 | paramCache.updatePhase(fluidState_, phaseIdx); | |
| 430 |
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62100240 | return FluidSystem::binaryDiffusionCoefficient(fluidState_, paramCache, phaseIdx, compIIdx, compJIdx); |
| 431 | } | ||
| 432 | |||
| 433 | /*! | ||
| 434 | * \brief Returns the effective diffusion coefficients for a phase in \f$[m^2/s]\f$. | ||
| 435 | */ | ||
| 436 | Scalar effectiveDiffusionCoefficient(int phaseIdx, int compIIdx, int compJIdx) const | ||
| 437 | 86105472 | { return effectiveDiffCoeff_(phaseIdx, compIIdx, compJIdx); } | |
| 438 | |||
| 439 | /*! | ||
| 440 | * \brief Returns the mass fraction of a component in the phase | ||
| 441 | * | ||
| 442 | * \param phaseIdx the index of the fluid phase | ||
| 443 | * \param compIdx the index of the component | ||
| 444 | */ | ||
| 445 | Scalar massFraction(int phaseIdx, int compIdx) const | ||
| 446 |
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174625480 | { return fluidState_.massFraction(phaseIdx, compIdx); } |
| 447 | |||
| 448 | /*! | ||
| 449 | * \brief Returns the mole fraction of a component in the phase | ||
| 450 | * | ||
| 451 | * \param phaseIdx the index of the fluid phase | ||
| 452 | * \param compIdx the index of the component | ||
| 453 | */ | ||
| 454 | Scalar moleFraction(int phaseIdx, int compIdx) const | ||
| 455 |
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845511600 | { return fluidState_.moleFraction(phaseIdx, compIdx); } |
| 456 | |||
| 457 | /*! | ||
| 458 | * \brief Returns the wetting phase index | ||
| 459 | */ | ||
| 460 | int wettingPhase() const | ||
| 461 | { return fluidState_.wettingPhase(); } | ||
| 462 | |||
| 463 | protected: | ||
| 464 | FluidState fluidState_; | ||
| 465 | SolidState solidState_; | ||
| 466 | |||
| 467 | private: | ||
| 468 | |||
| 469 | Scalar pc_; // The capillary pressure | ||
| 470 | Scalar porosity_; // Effective porosity within the control volume | ||
| 471 | PermeabilityType permeability_; // Effective permeability within the control volume | ||
| 472 | Scalar mobility_[ModelTraits::numFluidPhases()]; // Effective mobility within the control volume | ||
| 473 | DiffusionCoefficients effectiveDiffCoeff_; | ||
| 474 | |||
| 475 | }; | ||
| 476 | |||
| 477 | } // end namespace Dumux | ||
| 478 | |||
| 479 | #endif | ||
| 480 |