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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 CO2Model | ||
| 10 | * \brief Contains the quantities which are constant within a | ||
| 11 | * finite volume in the CO2 model. | ||
| 12 | */ | ||
| 13 | |||
| 14 | #ifndef DUMUX_CO2_VOLUME_VARIABLES_HH | ||
| 15 | #define DUMUX_CO2_VOLUME_VARIABLES_HH | ||
| 16 | |||
| 17 | #include <array> | ||
| 18 | |||
| 19 | #include <dune/common/exceptions.hh> | ||
| 20 | |||
| 21 | #include <dumux/porousmediumflow/volumevariables.hh> | ||
| 22 | #include <dumux/porousmediumflow/2p/formulation.hh> | ||
| 23 | #include <dumux/porousmediumflow/nonisothermal/volumevariables.hh> | ||
| 24 | #include <dumux/material/solidstates/updatesolidvolumefractions.hh> | ||
| 25 | |||
| 26 | #include "primaryvariableswitch.hh" | ||
| 27 | |||
| 28 | namespace Dumux { | ||
| 29 | |||
| 30 | /*! | ||
| 31 | * \ingroup CO2Model | ||
| 32 | * \brief Contains the quantities which are are constant within a | ||
| 33 | * finite volume in the CO2 model. | ||
| 34 | */ | ||
| 35 | template <class Traits> | ||
| 36 |
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57797631 | class TwoPTwoCCO2VolumeVariables |
| 37 | : public PorousMediumFlowVolumeVariables<Traits> | ||
| 38 | , public EnergyVolumeVariables<Traits, TwoPTwoCCO2VolumeVariables<Traits> > | ||
| 39 | { | ||
| 40 | using ParentType = PorousMediumFlowVolumeVariables< Traits>; | ||
| 41 | using EnergyVolVars = EnergyVolumeVariables<Traits, TwoPTwoCCO2VolumeVariables<Traits> >; | ||
| 42 | |||
| 43 | using Scalar = typename Traits::PrimaryVariables::value_type; | ||
| 44 | using ModelTraits = typename Traits::ModelTraits; | ||
| 45 | static constexpr int numFluidComps = ParentType::numFluidComponents(); | ||
| 46 | |||
| 47 | // component indices | ||
| 48 | enum | ||
| 49 | { | ||
| 50 | comp0Idx = Traits::FluidSystem::comp0Idx, | ||
| 51 | comp1Idx = Traits::FluidSystem::comp1Idx, | ||
| 52 | phase0Idx = Traits::FluidSystem::phase0Idx, | ||
| 53 | phase1Idx = Traits::FluidSystem::phase1Idx | ||
| 54 | }; | ||
| 55 | |||
| 56 | // phase presence indices | ||
| 57 | enum | ||
| 58 | { | ||
| 59 | firstPhaseOnly = ModelTraits::Indices::firstPhaseOnly, | ||
| 60 | secondPhaseOnly = ModelTraits::Indices::secondPhaseOnly, | ||
| 61 | bothPhases = ModelTraits::Indices::bothPhases | ||
| 62 | }; | ||
| 63 | |||
| 64 | // primary variable indices | ||
| 65 | enum | ||
| 66 | { | ||
| 67 | switchIdx = ModelTraits::Indices::switchIdx, | ||
| 68 | pressureIdx = ModelTraits::Indices::pressureIdx | ||
| 69 | }; | ||
| 70 | |||
| 71 | // formulation | ||
| 72 | static constexpr auto formulation = ModelTraits::priVarFormulation(); | ||
| 73 | |||
| 74 | // type used for the permeability | ||
| 75 | using PermeabilityType = typename Traits::PermeabilityType; | ||
| 76 | |||
| 77 | // type used for the diffusion coefficients | ||
| 78 | using EffDiffModel = typename Traits::EffectiveDiffusivityModel; | ||
| 79 | using DiffusionCoefficients = typename Traits::DiffusionType::DiffusionCoefficientsContainer; | ||
| 80 | |||
| 81 | public: | ||
| 82 | //! The type of the object returned by the fluidState() method | ||
| 83 | using FluidState = typename Traits::FluidState; | ||
| 84 | //! The fluid system used here | ||
| 85 | using FluidSystem = typename Traits::FluidSystem; | ||
| 86 | //! Export the indices | ||
| 87 | using Indices = typename ModelTraits::Indices; | ||
| 88 | //! Export type of solid state | ||
| 89 | using SolidState = typename Traits::SolidState; | ||
| 90 | //! Export type of solid system | ||
| 91 | using SolidSystem = typename Traits::SolidSystem; | ||
| 92 | //! Export the type of the primary variable switch | ||
| 93 | using PrimaryVariableSwitch = TwoPTwoCCO2PrimaryVariableSwitch; | ||
| 94 | |||
| 95 | |||
| 96 | //! Return whether moles or masses are balanced | ||
| 97 | static constexpr bool useMoles() { return ModelTraits::useMoles(); } | ||
| 98 | //! Return the two-phase formulation used here | ||
| 99 | static constexpr TwoPFormulation priVarFormulation() { return formulation; } | ||
| 100 | |||
| 101 | // check for permissive combinations | ||
| 102 | static_assert(ModelTraits::numFluidPhases() == 2, "NumPhases set in the model is not two!"); | ||
| 103 | static_assert(ModelTraits::numFluidComponents() == 2, "NumComponents set in the model is not two!"); | ||
| 104 | static_assert((formulation == TwoPFormulation::p0s1 || formulation == TwoPFormulation::p1s0), "Chosen TwoPFormulation not supported!"); | ||
| 105 | |||
| 106 | /*! | ||
| 107 | * \brief Updates all quantities for a given control volume. | ||
| 108 | * | ||
| 109 | * \param elemSol A vector containing all primary variables connected to the element | ||
| 110 | * \param problem The object specifying the problem which ought to | ||
| 111 | * be simulated | ||
| 112 | * \param element An element which contains part of the control volume | ||
| 113 | * \param scv The sub control volume | ||
| 114 | */ | ||
| 115 | template<class ElemSol, class Problem, class Element, class Scv> | ||
| 116 | 71188461 | void update(const ElemSol& elemSol, const Problem& problem, const Element& element, const Scv& scv) | |
| 117 | { | ||
| 118 | 71188461 | ParentType::update(elemSol, problem, element, scv); | |
| 119 | 71188461 | completeFluidState(elemSol, problem, element, scv, fluidState_, solidState_); | |
| 120 | |||
| 121 | // Second instance of a parameter cache. Could be avoided if | ||
| 122 | // diffusion coefficients also became part of the fluid state. | ||
| 123 | typename FluidSystem::ParameterCache paramCache; | ||
| 124 | 71188461 | paramCache.updateAll(fluidState_); | |
| 125 | |||
| 126 | 71188461 | const auto& spatialParams = problem.spatialParams(); | |
| 127 | 71188461 | const auto fluidMatrixInteraction = spatialParams.fluidMatrixInteraction(element, scv, elemSol); | |
| 128 | |||
| 129 | 71188461 | const int wPhaseIdx = fluidState_.wettingPhase(); | |
| 130 | 71188461 | const int nPhaseIdx = 1 - wPhaseIdx; | |
| 131 | |||
| 132 | // relative permeabilities -> require wetting phase saturation as parameter! | ||
| 133 | 71188461 | relativePermeability_[wPhaseIdx] = fluidMatrixInteraction.krw(saturation(wPhaseIdx)); | |
| 134 | 71188461 | relativePermeability_[nPhaseIdx] = fluidMatrixInteraction.krn(saturation(wPhaseIdx)); | |
| 135 | |||
| 136 | // porosity & permeabilty | ||
| 137 | 71188461 | updateSolidVolumeFractions(elemSol, problem, element, scv, solidState_, numFluidComps); | |
| 138 | 71188461 | EnergyVolVars::updateSolidEnergyParams(elemSol, problem, element, scv, solidState_); | |
| 139 | 71188461 | permeability_ = spatialParams.permeability(element, scv, elemSol); | |
| 140 | |||
| 141 | 71188461 | auto getEffectiveDiffusionCoefficient = [&](int phaseIdx, int compIIdx, int compJIdx) | |
| 142 | { | ||
| 143 | 142376922 | return EffDiffModel::effectiveDiffusionCoefficient(*this, phaseIdx, compIIdx, compJIdx); | |
| 144 | }; | ||
| 145 | |||
| 146 | 71188461 | effectiveDiffCoeff_.update(getEffectiveDiffusionCoefficient); | |
| 147 | |||
| 148 | 71188461 | EnergyVolVars::updateEffectiveThermalConductivity(); | |
| 149 | 71188461 | } | |
| 150 | |||
| 151 | /*! | ||
| 152 | * \brief Completes the fluid state. | ||
| 153 | * | ||
| 154 | * \note TODO: This is a lot of copy paste from the 2p2c: factor out code! | ||
| 155 | * | ||
| 156 | * \param elemSol A vector containing all primary variables connected to the element | ||
| 157 | * \param problem The object specifying the problem which ought to be simulated | ||
| 158 | * \param element An element which contains part of the control volume | ||
| 159 | * \param scv The sub-control volume | ||
| 160 | * \param fluidState A container with the current (physical) state of the fluid | ||
| 161 | * \param solidState A container with the current (physical) state of the solid | ||
| 162 | * | ||
| 163 | * Set temperature, saturations, capillary pressures, viscosities, densities and enthalpies. | ||
| 164 | */ | ||
| 165 | template<class ElemSol, class Problem, class Element, class Scv> | ||
| 166 | 71188461 | void completeFluidState(const ElemSol& elemSol, | |
| 167 | const Problem& problem, | ||
| 168 | const Element& element, | ||
| 169 | const Scv& scv, | ||
| 170 | FluidState& fluidState, | ||
| 171 | SolidState& solidState) | ||
| 172 | { | ||
| 173 | 71188461 | EnergyVolVars::updateTemperature(elemSol, problem, element, scv, fluidState, solidState); | |
| 174 | |||
| 175 | 71188461 | const auto& priVars = elemSol[scv.localDofIndex()]; | |
| 176 | 71188461 | const auto phasePresence = priVars.state(); | |
| 177 | |||
| 178 |
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71188461 | const auto& spatialParams = problem.spatialParams(); |
| 179 |
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71188461 | const auto wPhaseIdx = spatialParams.template wettingPhase<FluidSystem>(element, scv, elemSol); |
| 180 |
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71188461 | fluidState.setWettingPhase(wPhaseIdx); |
| 181 | |||
| 182 |
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71188461 | const auto fluidMatrixInteraction = spatialParams.fluidMatrixInteraction(element, scv, elemSol); |
| 183 | |||
| 184 | // set the saturations | ||
| 185 |
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71188461 | if (phasePresence == secondPhaseOnly) |
| 186 | { | ||
| 187 | ✗ | fluidState.setSaturation(phase0Idx, 0.0); | |
| 188 | ✗ | fluidState.setSaturation(phase1Idx, 1.0); | |
| 189 | } | ||
| 190 |
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71188461 | else if (phasePresence == firstPhaseOnly) |
| 191 | { | ||
| 192 | 67861748 | fluidState.setSaturation(phase0Idx, 1.0); | |
| 193 | 67861748 | fluidState.setSaturation(phase1Idx, 0.0); | |
| 194 | } | ||
| 195 |
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3326713 | else if (phasePresence == bothPhases) |
| 196 | { | ||
| 197 | if (formulation == TwoPFormulation::p0s1) | ||
| 198 | { | ||
| 199 | 6653426 | fluidState.setSaturation(phase1Idx, priVars[switchIdx]); | |
| 200 | 6653426 | fluidState.setSaturation(phase0Idx, 1 - priVars[switchIdx]); | |
| 201 | } | ||
| 202 | else | ||
| 203 | { | ||
| 204 | fluidState.setSaturation(phase0Idx, priVars[switchIdx]); | ||
| 205 | fluidState.setSaturation(phase1Idx, 1 - priVars[switchIdx]); | ||
| 206 | } | ||
| 207 | } | ||
| 208 | else | ||
| 209 | ✗ | DUNE_THROW(Dune::InvalidStateException, "Invalid phase presence."); | |
| 210 | |||
| 211 | // set pressures of the fluid phases | ||
| 212 | 142376922 | pc_ = fluidMatrixInteraction.pc(fluidState.saturation(wPhaseIdx)); | |
| 213 | if (formulation == TwoPFormulation::p0s1) | ||
| 214 | { | ||
| 215 |
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142376922 | fluidState.setPressure(phase0Idx, priVars[pressureIdx]); |
| 216 |
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142376922 | fluidState.setPressure(phase1Idx, (wPhaseIdx == phase0Idx) ? priVars[pressureIdx] + pc_ |
| 217 | : priVars[pressureIdx] - pc_); | ||
| 218 | } | ||
| 219 | else | ||
| 220 | { | ||
| 221 | fluidState.setPressure(phase1Idx, priVars[pressureIdx]); | ||
| 222 | fluidState.setPressure(phase0Idx, (wPhaseIdx == phase0Idx) ? priVars[pressureIdx] - pc_ | ||
| 223 | : priVars[pressureIdx] + pc_); | ||
| 224 | } | ||
| 225 | |||
| 226 | // calculate the phase compositions | ||
| 227 | typename FluidSystem::ParameterCache paramCache; | ||
| 228 | // both phases are present | ||
| 229 |
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71188461 | if (phasePresence == bothPhases) |
| 230 | { | ||
| 231 | //Get the equilibrium mole fractions from the FluidSystem and set them in the fluidState | ||
| 232 | //xCO2 = equilibrium mole fraction of CO2 in the liquid phase | ||
| 233 | //yH2O = equilibrium mole fraction of H2O in the gas phase | ||
| 234 | 3326713 | const auto xwCO2 = FluidSystem::equilibriumMoleFraction(fluidState, paramCache, phase0Idx); | |
| 235 | 3326713 | const auto xgH2O = FluidSystem::equilibriumMoleFraction(fluidState, paramCache, phase1Idx); | |
| 236 | 3326713 | const auto xwH2O = 1 - xwCO2; | |
| 237 | 3326713 | const auto xgCO2 = 1 - xgH2O; | |
| 238 | 3326713 | fluidState.setMoleFraction(phase0Idx, comp0Idx, xwH2O); | |
| 239 | 3326713 | fluidState.setMoleFraction(phase0Idx, comp1Idx, xwCO2); | |
| 240 | 3326713 | fluidState.setMoleFraction(phase1Idx, comp0Idx, xgH2O); | |
| 241 | 3326713 | fluidState.setMoleFraction(phase1Idx, comp1Idx, xgCO2); | |
| 242 | } | ||
| 243 | |||
| 244 | // only the nonwetting phase is present, i.e. nonwetting phase | ||
| 245 | // composition is stored explicitly. | ||
| 246 |
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67861748 | else if (phasePresence == secondPhaseOnly) |
| 247 | { | ||
| 248 | if( useMoles() ) // mole-fraction formulation | ||
| 249 | { | ||
| 250 | // set the fluid state | ||
| 251 | fluidState.setMoleFraction(phase1Idx, comp0Idx, priVars[switchIdx]); | ||
| 252 | fluidState.setMoleFraction(phase1Idx, comp1Idx, 1-priVars[switchIdx]); | ||
| 253 | // TODO give values for non-existing wetting phase | ||
| 254 | const auto xwCO2 = FluidSystem::equilibriumMoleFraction(fluidState, paramCache, phase0Idx); | ||
| 255 | const auto xwH2O = 1 - xwCO2; | ||
| 256 | fluidState.setMoleFraction(phase0Idx, comp1Idx, xwCO2); | ||
| 257 | fluidState.setMoleFraction(phase0Idx, comp0Idx, xwH2O); | ||
| 258 | } | ||
| 259 | else // mass-fraction formulation | ||
| 260 | { | ||
| 261 | // setMassFraction() has only to be called 1-numComponents times | ||
| 262 | ✗ | fluidState.setMassFraction(phase1Idx, comp0Idx, priVars[switchIdx]); | |
| 263 | // TODO give values for non-existing wetting phase | ||
| 264 | ✗ | const auto xwCO2 = FluidSystem::equilibriumMoleFraction(fluidState, paramCache, phase0Idx); | |
| 265 | ✗ | const auto xwH2O = 1 - xwCO2; | |
| 266 | ✗ | fluidState.setMoleFraction(phase0Idx, comp1Idx, xwCO2); | |
| 267 | ✗ | fluidState.setMoleFraction(phase0Idx, comp0Idx, xwH2O); | |
| 268 | } | ||
| 269 | } | ||
| 270 | |||
| 271 | // only the wetting phase is present, i.e. wetting phase | ||
| 272 | // composition is stored explicitly. | ||
| 273 |
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67861748 | else if (phasePresence == firstPhaseOnly) |
| 274 | { | ||
| 275 | if( useMoles() ) // mole-fraction formulation | ||
| 276 | { | ||
| 277 | // convert mass to mole fractions and set the fluid state | ||
| 278 | fluidState.setMoleFraction(phase0Idx, comp0Idx, 1-priVars[switchIdx]); | ||
| 279 | fluidState.setMoleFraction(phase0Idx, comp1Idx, priVars[switchIdx]); | ||
| 280 | // TODO give values for non-existing nonwetting phase | ||
| 281 | Scalar xnH2O = FluidSystem::equilibriumMoleFraction(fluidState, paramCache, phase1Idx); | ||
| 282 | Scalar xnCO2 = 1 - xnH2O; | ||
| 283 | fluidState.setMoleFraction(phase1Idx, comp1Idx, xnCO2); | ||
| 284 | fluidState.setMoleFraction(phase1Idx, comp0Idx, xnH2O); | ||
| 285 | } | ||
| 286 | else // mass-fraction formulation | ||
| 287 | { | ||
| 288 | // setMassFraction() has only to be called 1-numComponents times | ||
| 289 | 135723496 | fluidState.setMassFraction(phase0Idx, comp1Idx, priVars[switchIdx]); | |
| 290 | // TODO give values for non-existing nonwetting phase | ||
| 291 | 67861748 | Scalar xnH2O = FluidSystem::equilibriumMoleFraction(fluidState, paramCache, phase1Idx); | |
| 292 | 67861748 | Scalar xnCO2 = 1 - xnH2O; | |
| 293 | 67861748 | fluidState.setMoleFraction(phase1Idx, comp1Idx, xnCO2); | |
| 294 | 67861748 | fluidState.setMoleFraction(phase1Idx, comp0Idx, xnH2O); | |
| 295 | } | ||
| 296 | } | ||
| 297 | |||
| 298 |
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213565383 | for (int phaseIdx = 0; phaseIdx < ModelTraits::numFluidPhases(); ++phaseIdx) |
| 299 | { | ||
| 300 | // set the viscosity and desity here if constraintsolver is not used | ||
| 301 | 142376922 | paramCache.updateComposition(fluidState, phaseIdx); | |
| 302 | 142376922 | const Scalar rho = FluidSystem::density(fluidState, paramCache, phaseIdx); | |
| 303 | 142376922 | fluidState.setDensity(phaseIdx, rho); | |
| 304 | 142376922 | const Scalar rhoMolar = FluidSystem::molarDensity(fluidState, phaseIdx); | |
| 305 | 142376922 | fluidState.setMolarDensity(phaseIdx, rhoMolar); | |
| 306 | 142376922 | const Scalar mu = FluidSystem::viscosity(fluidState, paramCache, phaseIdx); | |
| 307 | 142376922 | fluidState.setViscosity(phaseIdx,mu); | |
| 308 | |||
| 309 | // compute and set the enthalpy | ||
| 310 | 142376922 | Scalar h = EnergyVolVars::enthalpy(fluidState, paramCache, phaseIdx); | |
| 311 | 284753844 | fluidState.setEnthalpy(phaseIdx, h); | |
| 312 | } | ||
| 313 | 71188461 | } | |
| 314 | |||
| 315 | /*! | ||
| 316 | * \brief Returns the phase state within the control volume. | ||
| 317 | */ | ||
| 318 | const FluidState &fluidState() const | ||
| 319 | 742787357 | { return fluidState_; } | |
| 320 | |||
| 321 | /*! | ||
| 322 | * \brief Returns the phase state for the control volume. | ||
| 323 | */ | ||
| 324 | const SolidState &solidState() const | ||
| 325 | 46343514 | { return solidState_; } | |
| 326 | |||
| 327 | /*! | ||
| 328 | * \brief Returns the average molar mass \f$\mathrm{[kg/mol]}\f$ of the fluid phase. | ||
| 329 | * | ||
| 330 | * \param phaseIdx The phase index | ||
| 331 | */ | ||
| 332 | Scalar averageMolarMass(int phaseIdx) const | ||
| 333 | { return fluidState_.averageMolarMass(phaseIdx); } | ||
| 334 | |||
| 335 | /*! | ||
| 336 | * \brief Returns the saturation of a given phase within | ||
| 337 | * the control volume in \f$[-]\f$. | ||
| 338 | * | ||
| 339 | * \param phaseIdx The phase index | ||
| 340 | */ | ||
| 341 | Scalar saturation(const int phaseIdx) const | ||
| 342 |
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2964213248 | { return fluidState_.saturation(phaseIdx); } |
| 343 | |||
| 344 | /*! | ||
| 345 | * \brief Returns the mass fraction of a given component in a | ||
| 346 | * given phase within the control volume in \f$[-]\f$. | ||
| 347 | * | ||
| 348 | * \param phaseIdx The phase index | ||
| 349 | * \param compIdx The component index | ||
| 350 | */ | ||
| 351 | Scalar massFraction(const int phaseIdx, const int compIdx) const | ||
| 352 | 4302283120 | { return fluidState_.massFraction(phaseIdx, compIdx); } | |
| 353 | |||
| 354 | /*! | ||
| 355 | * \brief Returns the mole fraction of a given component in a | ||
| 356 | * given phase within the control volume in \f$[-]\f$. | ||
| 357 | * | ||
| 358 | * \param phaseIdx The phase index | ||
| 359 | * \param compIdx The component index | ||
| 360 | */ | ||
| 361 | Scalar moleFraction(const int phaseIdx, const int compIdx) const | ||
| 362 | 11882086 | { return fluidState_.moleFraction(phaseIdx, compIdx); } | |
| 363 | |||
| 364 | /*! | ||
| 365 | * \brief Returns the mass density of a given phase within the | ||
| 366 | * control volume in \f$[kg/m^3]\f$. | ||
| 367 | * | ||
| 368 | * \param phaseIdx The phase index | ||
| 369 | */ | ||
| 370 | Scalar density(const int phaseIdx) const | ||
| 371 |
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13561004512 | { return fluidState_.density(phaseIdx); } |
| 372 | |||
| 373 | /*! | ||
| 374 | * \brief Returns the dynamic viscosity of the fluid within the | ||
| 375 | * control volume in \f$\mathrm{[Pa s]}\f$. | ||
| 376 | * | ||
| 377 | * \param phaseIdx The phase index | ||
| 378 | */ | ||
| 379 | Scalar viscosity(const int phaseIdx) const | ||
| 380 | { return fluidState_.viscosity(phaseIdx); } | ||
| 381 | |||
| 382 | /*! | ||
| 383 | * \brief Returns the mass density of a given phase within the | ||
| 384 | * control volume in \f$[mol/m^3]\f$. | ||
| 385 | * | ||
| 386 | * \param phaseIdx The phase index | ||
| 387 | */ | ||
| 388 | Scalar molarDensity(const int phaseIdx) const | ||
| 389 | 9358184 | { return fluidState_.molarDensity(phaseIdx) ; } | |
| 390 | |||
| 391 | /*! | ||
| 392 | * \brief Returns the effective pressure of a given phase within | ||
| 393 | * the control volume in \f$[kg/(m*s^2)=N/m^2=Pa]\f$. | ||
| 394 | * | ||
| 395 | * \param phaseIdx The phase index | ||
| 396 | */ | ||
| 397 | Scalar pressure(const int phaseIdx) const | ||
| 398 | 2456955800 | { return fluidState_.pressure(phaseIdx); } | |
| 399 | |||
| 400 | /*! | ||
| 401 | * \brief Returns temperature within the control volume in \f$[K]\f$. | ||
| 402 | * | ||
| 403 | * Note that we assume thermodynamic equilibrium, i.e. the | ||
| 404 | * temperature of the rock matrix and of all fluid phases are | ||
| 405 | * identical. | ||
| 406 | */ | ||
| 407 | Scalar temperature() const | ||
| 408 |
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670965024 | { return fluidState_.temperature(/*phaseIdx=*/0); } |
| 409 | |||
| 410 | /*! | ||
| 411 | * \brief Returns the relative permeability of a given phase within | ||
| 412 | * the control volume in \f$[-]\f$. | ||
| 413 | * | ||
| 414 | * \param phaseIdx The phase index | ||
| 415 | */ | ||
| 416 | Scalar relativePermeability(const int phaseIdx) const | ||
| 417 | { return relativePermeability_[phaseIdx]; } | ||
| 418 | |||
| 419 | /*! | ||
| 420 | * \brief Returns the effective mobility of a given phase within | ||
| 421 | * the control volume in \f$[s*m/kg]\f$. | ||
| 422 | * | ||
| 423 | * \param phaseIdx The phase index | ||
| 424 | */ | ||
| 425 | Scalar mobility(const int phaseIdx) const | ||
| 426 | 1237192560 | { return relativePermeability_[phaseIdx]/fluidState_.viscosity(phaseIdx); } | |
| 427 | |||
| 428 | /*! | ||
| 429 | * \brief Returns the effective capillary pressure within the control volume | ||
| 430 | * in \f$[kg/(m*s^2)=N/m^2=Pa]\f$. | ||
| 431 | */ | ||
| 432 | Scalar capillaryPressure() const | ||
| 433 | 7018638 | { return fluidState_.pressure(phase1Idx) - fluidState_.pressure(phase0Idx); } | |
| 434 | |||
| 435 | /*! | ||
| 436 | * \brief Returns the average porosity within the control volume in \f$[-]\f$. | ||
| 437 | */ | ||
| 438 | Scalar porosity() const | ||
| 439 |
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2821247016 | { return solidState_.porosity(); } |
| 440 | |||
| 441 | /*! | ||
| 442 | * \brief Returns the average permeability within the control volume in \f$[m^2]\f$. | ||
| 443 | */ | ||
| 444 | const PermeabilityType& permeability() const | ||
| 445 | ✗ | { return permeability_; } | |
| 446 | |||
| 447 | /*! | ||
| 448 | * \brief Returns the binary diffusion coefficients for a phase in \f$[m^2/s]\f$. | ||
| 449 | */ | ||
| 450 | Scalar diffusionCoefficient(int phaseIdx, int compIIdx, int compJIdx) const | ||
| 451 | { | ||
| 452 | typename FluidSystem::ParameterCache paramCache; | ||
| 453 | 142376922 | paramCache.updatePhase(fluidState_, phaseIdx); | |
| 454 |
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142376922 | return FluidSystem::binaryDiffusionCoefficient(fluidState_, paramCache, phaseIdx, compIIdx, compJIdx); |
| 455 | } | ||
| 456 | |||
| 457 | /*! | ||
| 458 | * \brief Returns the effective diffusion coefficients for a phase in \f$[m^2/s]\f$. | ||
| 459 | */ | ||
| 460 | Scalar effectiveDiffusionCoefficient(int phaseIdx, int compIIdx, int compJIdx) const | ||
| 461 | 708889568 | { return effectiveDiffCoeff_(phaseIdx, compIIdx, compJIdx); } | |
| 462 | |||
| 463 | |||
| 464 | /*! | ||
| 465 | * \brief Returns the wetting phase index | ||
| 466 | */ | ||
| 467 | int wettingPhase() const | ||
| 468 | { return fluidState_.wettingPhase(); } | ||
| 469 | |||
| 470 | private: | ||
| 471 | FluidState fluidState_; | ||
| 472 | SolidState solidState_; | ||
| 473 | Scalar pc_; // The capillary pressure | ||
| 474 | PermeabilityType permeability_; // Effective permeability within the control volume | ||
| 475 | |||
| 476 | // Relative permeability within the control volume | ||
| 477 | std::array<Scalar, ModelTraits::numFluidPhases()> relativePermeability_; | ||
| 478 | |||
| 479 | // Effective diffusion coefficients for the phases | ||
| 480 | DiffusionCoefficients effectiveDiffCoeff_; | ||
| 481 | }; | ||
| 482 | |||
| 483 | } // end namespace Dumux | ||
| 484 | |||
| 485 | #endif | ||
| 486 |