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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-FileCopyrightText: 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 FreeflowNCModel | ||
| 10 | * | ||
| 11 | * \copydoc Dumux::FreeflowNCVolumeVariables | ||
| 12 | */ | ||
| 13 | #ifndef DUMUX_FREEFLOW_NC_VOLUMEVARIABLES_HH | ||
| 14 | #define DUMUX_FREEFLOW_NC_VOLUMEVARIABLES_HH | ||
| 15 | |||
| 16 | #include <array> | ||
| 17 | #include <dune/common/exceptions.hh> | ||
| 18 | #include <dumux/freeflow/volumevariables.hh> | ||
| 19 | |||
| 20 | namespace Dumux { | ||
| 21 | |||
| 22 | /*! | ||
| 23 | * \ingroup FreeflowNCModel | ||
| 24 | * \brief Volume variables for the single-phase, multi-component free-flow model. | ||
| 25 | */ | ||
| 26 | template <class Traits> | ||
| 27 |
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91058 | class FreeflowNCVolumeVariables : public FreeFlowVolumeVariables< Traits, FreeflowNCVolumeVariables<Traits> > |
| 28 | { | ||
| 29 | using ThisType = FreeflowNCVolumeVariables<Traits>; | ||
| 30 | using ParentType = FreeFlowVolumeVariables<Traits, ThisType>; | ||
| 31 | |||
| 32 | using Scalar = typename Traits::PrimaryVariables::value_type; | ||
| 33 | |||
| 34 | static constexpr bool useMoles = Traits::ModelTraits::useMoles(); | ||
| 35 | static constexpr int numFluidComps = ParentType::numFluidComponents(); | ||
| 36 | using DiffusionCoefficients = typename Traits::DiffusionType::DiffusionCoefficientsContainer; | ||
| 37 | |||
| 38 | public: | ||
| 39 | //! export the underlying fluid system | ||
| 40 | using FluidSystem = typename Traits::FluidSystem; | ||
| 41 | //! export the fluid state type | ||
| 42 | using FluidState = typename Traits::FluidState; | ||
| 43 | //! export the indices type | ||
| 44 | using Indices = typename Traits::ModelTraits::Indices; | ||
| 45 | |||
| 46 | /*! | ||
| 47 | * \brief Update all quantities for a given control volume | ||
| 48 | * | ||
| 49 | * \param elemSol A vector containing all primary variables connected to the element | ||
| 50 | * \param problem The object specifying the problem which ought to | ||
| 51 | * be simulated | ||
| 52 | * \param element An element which contains part of the control volume | ||
| 53 | * \param scv The sub-control volume | ||
| 54 | */ | ||
| 55 | template<class ElementSolution, class Problem, class Element, class SubControlVolume> | ||
| 56 | 40941936 | void update(const ElementSolution &elemSol, | |
| 57 | const Problem &problem, | ||
| 58 | const Element &element, | ||
| 59 | const SubControlVolume& scv) | ||
| 60 | { | ||
| 61 | 40941936 | ParentType::update(elemSol, problem, element, scv); | |
| 62 | |||
| 63 | 40941936 | completeFluidState(elemSol, problem, element, scv, fluidState_); | |
| 64 | |||
| 65 | typename FluidSystem::ParameterCache paramCache; | ||
| 66 | paramCache.updateAll(fluidState_); | ||
| 67 | |||
| 68 | 84004962 | auto getDiffusionCoefficient = [&](int phaseIdx, int compIIdx, int compJIdx) | |
| 69 | { | ||
| 70 | 43063026 | return FluidSystem::binaryDiffusionCoefficient(this->fluidState_, | |
| 71 | paramCache, | ||
| 72 | 0, | ||
| 73 | compIIdx, | ||
| 74 | compJIdx); | ||
| 75 | }; | ||
| 76 | |||
| 77 | 40941936 | diffCoefficient_.update(getDiffusionCoefficient); | |
| 78 | 40941936 | } | |
| 79 | |||
| 80 | /*! | ||
| 81 | * \brief Update the fluid state | ||
| 82 | */ | ||
| 83 | template<class ElementSolution, class Problem, class Element, class SubControlVolume> | ||
| 84 | 40941936 | static void completeFluidState(const ElementSolution& elemSol, | |
| 85 | const Problem& problem, | ||
| 86 | const Element& element, | ||
| 87 | const SubControlVolume& scv, | ||
| 88 | FluidState& fluidState) | ||
| 89 | { | ||
| 90 | 40941936 | fluidState.setTemperature(ParentType::temperature(elemSol, problem, element, scv)); | |
| 91 | 40941936 | fluidState.setPressure(0, elemSol[0][Indices::pressureIdx]); | |
| 92 | |||
| 93 | // saturation in a single phase is always 1 and thus redundant | ||
| 94 | // to set. But since we use the fluid state shared by the | ||
| 95 | // immiscible multi-phase models, so we have to set it here... | ||
| 96 | 40941936 | fluidState.setSaturation(0, 1.0); | |
| 97 | |||
| 98 | 40941936 | Scalar sumFracMinorComp = 0.0; | |
| 99 | |||
| 100 |
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82945392 | for(int compIdx = 1; compIdx < ParentType::numFluidComponents(); ++compIdx) |
| 101 | { | ||
| 102 | // temporary add 1.0 to remove spurious differences in mole fractions | ||
| 103 | // which are below the numerical accuracy | ||
| 104 | 42003456 | Scalar moleOrMassFraction = elemSol[0][Indices::conti0EqIdx+compIdx] + 1.0; | |
| 105 | 42003456 | moleOrMassFraction = moleOrMassFraction - 1.0; | |
| 106 | if(useMoles) | ||
| 107 | 41999556 | fluidState.setMoleFraction(0, compIdx, moleOrMassFraction); | |
| 108 | else | ||
| 109 | 3900 | fluidState.setMassFraction(0, compIdx, moleOrMassFraction); | |
| 110 | 42003456 | sumFracMinorComp += moleOrMassFraction; | |
| 111 | } | ||
| 112 | if(useMoles) | ||
| 113 | 40938036 | fluidState.setMoleFraction(0, 0, 1.0 - sumFracMinorComp); | |
| 114 | else | ||
| 115 | 3900 | fluidState.setMassFraction(0, 0, 1.0 - sumFracMinorComp); | |
| 116 | |||
| 117 | typename FluidSystem::ParameterCache paramCache; | ||
| 118 | 40941936 | paramCache.updateAll(fluidState); | |
| 119 | |||
| 120 | 40941936 | Scalar value = FluidSystem::density(fluidState, paramCache, 0); | |
| 121 | 40941936 | fluidState.setDensity(0, value); | |
| 122 | |||
| 123 | 40941936 | value = FluidSystem::molarDensity(fluidState, paramCache, 0); | |
| 124 | 40941936 | fluidState.setMolarDensity(0, value); | |
| 125 | |||
| 126 | 40941936 | value = FluidSystem::viscosity(fluidState, paramCache, 0); | |
| 127 | 40941936 | fluidState.setViscosity(0, value); | |
| 128 | |||
| 129 | // compute and set the enthalpy | ||
| 130 | 40941936 | const Scalar h = ParentType::enthalpy(fluidState, paramCache); | |
| 131 | 40941936 | fluidState.setEnthalpy(0, h); | |
| 132 | 40941936 | } | |
| 133 | |||
| 134 | /*! | ||
| 135 | * \brief Return the effective pressure \f$\mathrm{[Pa]}\f$ of a given phase within | ||
| 136 | * the control volume. | ||
| 137 | */ | ||
| 138 | 48955015 | Scalar pressure(int phaseIdx = 0) const | |
| 139 | 48735247 | { return fluidState_.pressure(0); } | |
| 140 | |||
| 141 | /*! | ||
| 142 | * \brief Return the mass density \f$\mathrm{[kg/m^3]}\f$ of a given phase within the | ||
| 143 | * control volume. | ||
| 144 | */ | ||
| 145 | 946656518 | Scalar density(int phaseIdx = 0) const | |
| 146 |
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889880325 | { return fluidState_.density(0); } |
| 147 | |||
| 148 | /*! | ||
| 149 | * \brief Return temperature \f$\mathrm{[K]}\f$ inside the sub-control volume. | ||
| 150 | * | ||
| 151 | * Note that we assume thermodynamic equilibrium, i.e. the | ||
| 152 | * temperatures of the rock matrix and of all fluid phases are | ||
| 153 | * identical. | ||
| 154 | */ | ||
| 155 | 25821102 | Scalar temperature() const | |
| 156 | 25714328 | { return fluidState_.temperature(); } | |
| 157 | |||
| 158 | /*! | ||
| 159 | * \brief Return the effective dynamic viscosity \f$\mathrm{[Pa s]}\f$ of the fluid within the | ||
| 160 | * control volume. | ||
| 161 | */ | ||
| 162 | 25845924 | Scalar effectiveViscosity() const | |
| 163 | 25845924 | { return viscosity(); } | |
| 164 | |||
| 165 | /*! | ||
| 166 | * \brief Return the dynamic viscosity \f$\mathrm{[Pa s]}\f$ of the fluid within the | ||
| 167 | * control volume. | ||
| 168 | */ | ||
| 169 | 225062714 | Scalar viscosity(int phaseIdx = 0) const | |
| 170 |
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210863340 | { return fluidState_.viscosity(0); } |
| 171 | |||
| 172 | /*! | ||
| 173 | * \brief Returns the mass fraction of a component in the phase \f$\mathrm{[-]}\f$ | ||
| 174 | * | ||
| 175 | * \param phaseIdx the index of the phase | ||
| 176 | * \param compIdx the index of the component | ||
| 177 | */ | ||
| 178 | 157212352 | Scalar massFraction(int phaseIdx, int compIdx) const | |
| 179 | 80846497 | { return fluidState_.massFraction(0, compIdx); } | |
| 180 | |||
| 181 | /*! | ||
| 182 | * \brief Returns the mass fraction of a component in the phase \f$\mathrm{[-]}\f$ | ||
| 183 | * | ||
| 184 | * \param compIdx the index of the component | ||
| 185 | */ | ||
| 186 | 282736 | Scalar massFraction(int compIdx) const | |
| 187 | 282736 | { return fluidState_.massFraction(0, compIdx); } | |
| 188 | |||
| 189 | /*! | ||
| 190 | * \brief Returns the mole fraction of a component in the phase \f$\mathrm{[-]}\f$ | ||
| 191 | * | ||
| 192 | * \param phaseIdx the index of the phase | ||
| 193 | * \param compIdx the index of the component | ||
| 194 | */ | ||
| 195 | 1222404 | Scalar moleFraction(int phaseIdx, int compIdx) const | |
| 196 |
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1051400 | { return fluidState_.moleFraction(0, compIdx); } |
| 197 | |||
| 198 | /*! | ||
| 199 | * \brief Returns the mole fraction of a component in the phase \f$\mathrm{[-]}\f$ | ||
| 200 | * | ||
| 201 | * \param compIdx the index of the component | ||
| 202 | */ | ||
| 203 | 206600952 | Scalar moleFraction(int compIdx) const | |
| 204 |
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206318816 | { return fluidState_.moleFraction(0, compIdx); } |
| 205 | |||
| 206 | /*! | ||
| 207 | * \brief Returns the mass density of a given phase \f$\mathrm{[kg/m^3]}\f$ | ||
| 208 | */ | ||
| 209 | 149494036 | Scalar molarDensity(int phaseIdx = 0) const | |
| 210 |
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149356168 | { return fluidState_.molarDensity(0); } |
| 211 | |||
| 212 | /*! | ||
| 213 | * \brief Returns the molar mass of a given component. | ||
| 214 | * | ||
| 215 | * \param compIdx the index of the component | ||
| 216 | */ | ||
| 217 | Scalar molarMass(int compIdx) const | ||
| 218 | { return FluidSystem::molarMass(compIdx); } | ||
| 219 | |||
| 220 | /*! | ||
| 221 | * \brief Returns the average molar mass \f$\mathrm{[kg/mol]}\f$ of the fluid phase. | ||
| 222 | * | ||
| 223 | * \param phaseIdx The phase index | ||
| 224 | */ | ||
| 225 | 8456080 | Scalar averageMolarMass(const int phaseIdx = 0) const | |
| 226 | 8456080 | { return fluidState_.averageMolarMass(phaseIdx); } | |
| 227 | |||
| 228 | /*! | ||
| 229 | * \brief Returns the binary diffusion coefficients for a phase in \f$[m^2/s]\f$. | ||
| 230 | */ | ||
| 231 | 182337653 | Scalar diffusionCoefficient(int phaseIdx, int compIIdx, int compJIdx) const | |
| 232 | 142853782 | { return diffCoefficient_(0, compIIdx, compJIdx); } | |
| 233 | |||
| 234 | /*! | ||
| 235 | * \brief Returns the effective diffusion coefficients for a phase in \f$[m^2/s]\f$. | ||
| 236 | */ | ||
| 237 | 39483871 | Scalar effectiveDiffusionCoefficient(int phaseIdx, int compIIdx, int compJIdx) const | |
| 238 |
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39483871 | { return diffusionCoefficient(0, compIIdx, compJIdx); } |
| 239 | |||
| 240 | /*! | ||
| 241 | * \brief Return the fluid state of the control volume. | ||
| 242 | */ | ||
| 243 | 70688752 | const FluidState& fluidState() const | |
| 244 |
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150777488 | { return fluidState_; } |
| 245 | |||
| 246 | protected: | ||
| 247 | FluidState fluidState_; | ||
| 248 | // Binary diffusion coefficient | ||
| 249 | DiffusionCoefficients diffCoefficient_; | ||
| 250 | }; | ||
| 251 | |||
| 252 | } // end namespace Dumux | ||
| 253 | |||
| 254 | #endif | ||
| 255 |