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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 NavierStokesModel | ||
| 10 | * | ||
| 11 | * \copydoc Dumux::NavierStokesVolumeVariables | ||
| 12 | */ | ||
| 13 | #ifndef DUMUX_NAVIERSTOKES_MASS_1PNC_VOLUME_VARIABLES_HH | ||
| 14 | #define DUMUX_NAVIERSTOKES_MASS_1PNC_VOLUME_VARIABLES_HH | ||
| 15 | |||
| 16 | #include <dumux/freeflow/navierstokes/scalarvolumevariables.hh> | ||
| 17 | #include <dumux/freeflow/navierstokes/energy/volumevariables.hh> | ||
| 18 | |||
| 19 | namespace Dumux { | ||
| 20 | |||
| 21 | /*! | ||
| 22 | * \ingroup NavierStokesModel | ||
| 23 | * \brief Volume variables for the single-phase Navier-Stokes model. | ||
| 24 | */ | ||
| 25 | template <class Traits> | ||
| 26 | 1190088 | class NavierStokesMassOnePNCVolumeVariables | |
| 27 | : public NavierStokesScalarConservationModelVolumeVariables<Traits> | ||
| 28 | , public NavierStokesEnergyVolumeVariables<Traits, NavierStokesMassOnePNCVolumeVariables<Traits>> | ||
| 29 | { | ||
| 30 | using ParentType = NavierStokesScalarConservationModelVolumeVariables<Traits>; | ||
| 31 | using EnergyVolumeVariables = NavierStokesEnergyVolumeVariables<Traits, NavierStokesMassOnePNCVolumeVariables<Traits>>; | ||
| 32 | |||
| 33 | using Scalar = typename Traits::PrimaryVariables::value_type; | ||
| 34 | |||
| 35 | static constexpr bool useMoles = Traits::ModelTraits::useMoles(); | ||
| 36 | using DiffusionCoefficients = typename Traits::DiffusionType::DiffusionCoefficientsContainer; | ||
| 37 | |||
| 38 | |||
| 39 | public: | ||
| 40 | //! export the underlying fluid system | ||
| 41 | using FluidSystem = typename Traits::FluidSystem; | ||
| 42 | //! export the fluid state type | ||
| 43 | using FluidState = typename Traits::FluidState; | ||
| 44 | //! export the diffusion type | ||
| 45 | using MolecularDiffusionType = typename Traits::DiffusionType; | ||
| 46 | //! export the indices type | ||
| 47 | using Indices = typename Traits::ModelTraits::Indices; | ||
| 48 | |||
| 49 | /*! | ||
| 50 | * \brief Update all quantities for a given control volume | ||
| 51 | * | ||
| 52 | * \param elemSol A vector containing all primary variables connected to the element | ||
| 53 | * \param problem The object specifying the problem which ought to | ||
| 54 | * be simulated | ||
| 55 | * \param element An element which contains part of the control volume | ||
| 56 | * \param scv The sub-control volume | ||
| 57 | */ | ||
| 58 | template<class ElementSolution, class Problem, class Element, class SubControlVolume> | ||
| 59 | 15258896 | void update(const ElementSolution &elemSol, | |
| 60 | const Problem &problem, | ||
| 61 | const Element &element, | ||
| 62 | const SubControlVolume& scv) | ||
| 63 | { | ||
| 64 | 15258896 | ParentType::update(elemSol, problem, element, scv); | |
| 65 | |||
| 66 | 15258896 | completeFluidState(elemSol, problem, element, scv, fluidState_); | |
| 67 | |||
| 68 | typename FluidSystem::ParameterCache paramCache; | ||
| 69 | 15258896 | paramCache.updateAll(fluidState_); | |
| 70 | |||
| 71 | 15258896 | auto getDiffusionCoefficient = [&](int phaseIdx, int compIIdx, int compJIdx) | |
| 72 | { | ||
| 73 | 16117496 | return FluidSystem::binaryDiffusionCoefficient(this->fluidState_, | |
| 74 | 16117496 | paramCache, | |
| 75 | 0, | ||
| 76 | compIIdx, | ||
| 77 | ✗ | compJIdx); | |
| 78 | }; | ||
| 79 | |||
| 80 | 15258896 | diffCoefficient_.update(getDiffusionCoefficient); | |
| 81 | 15258896 | EnergyVolumeVariables::updateEffectiveThermalConductivity(); | |
| 82 | 15258896 | } | |
| 83 | |||
| 84 | /*! | ||
| 85 | * \brief Update the fluid state | ||
| 86 | */ | ||
| 87 | template<class ElementSolution, class Problem, class Element, class SubControlVolume> | ||
| 88 | 15258896 | void completeFluidState(const ElementSolution& elemSol, | |
| 89 | const Problem& problem, | ||
| 90 | const Element& element, | ||
| 91 | const SubControlVolume& scv, | ||
| 92 | FluidState& fluidState) const | ||
| 93 | { | ||
| 94 | 20002211 | fluidState.setTemperature(0, EnergyVolumeVariables::getTemperature(elemSol, problem, element, scv)); | |
| 95 | 45776688 | fluidState.setPressure(0, elemSol[0][Indices::pressureIdx]); | |
| 96 | |||
| 97 | // saturation in a single phase is always 1 and thus redundant | ||
| 98 | // to set. But since we use the fluid state shared by the | ||
| 99 | // immiscible multi-phase models, so we have to set it here... | ||
| 100 | 15258896 | fluidState.setSaturation(0, 1.0); | |
| 101 | |||
| 102 | 15258896 | Scalar sumFracMinorComp = 0.0; | |
| 103 | |||
| 104 |
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30947092 | for(int compIdx = 1; compIdx < ParentType::numFluidComponents(); ++compIdx) |
| 105 | { | ||
| 106 | // temporary add 1.0 to remove spurious differences in mole fractions | ||
| 107 | // which are below the numerical accuracy | ||
| 108 | 31376392 | Scalar moleOrMassFraction = elemSol[0][Indices::conti0EqIdx+compIdx] + 1.0; | |
| 109 | 15688196 | moleOrMassFraction = moleOrMassFraction - 1.0; | |
| 110 | if(useMoles) | ||
| 111 | 15688196 | fluidState.setMoleFraction(0, compIdx, moleOrMassFraction); | |
| 112 | else | ||
| 113 | fluidState.setMassFraction(0, compIdx, moleOrMassFraction); | ||
| 114 | 15688196 | sumFracMinorComp += moleOrMassFraction; | |
| 115 | } | ||
| 116 | if(useMoles) | ||
| 117 | 15258896 | fluidState.setMoleFraction(0, 0, 1.0 - sumFracMinorComp); | |
| 118 | else | ||
| 119 | fluidState.setMassFraction(0, 0, 1.0 - sumFracMinorComp); | ||
| 120 | |||
| 121 | typename FluidSystem::ParameterCache paramCache; | ||
| 122 | 15258896 | paramCache.updateAll(fluidState); | |
| 123 | |||
| 124 | 15688196 | Scalar value = FluidSystem::density(fluidState, paramCache, 0); | |
| 125 | 15688196 | fluidState.setDensity(0, value); | |
| 126 | |||
| 127 | 15688196 | value = FluidSystem::molarDensity(fluidState, paramCache, 0); | |
| 128 | 15688196 | fluidState.setMolarDensity(0, value); | |
| 129 | |||
| 130 | 15688196 | value = FluidSystem::viscosity(fluidState, paramCache, 0); | |
| 131 | 25774477 | fluidState.setViscosity(0, value); | |
| 132 | |||
| 133 | // compute and set the enthalpy | ||
| 134 | 15258896 | const Scalar h = EnergyVolumeVariables::enthalpy(fluidState, paramCache); | |
| 135 | 30517792 | fluidState.setEnthalpy(0, h); | |
| 136 | 15258896 | } | |
| 137 | |||
| 138 | /*! | ||
| 139 | * \brief Return the effective pressure \f$\mathrm{[Pa]}\f$ of a given phase within | ||
| 140 | * the control volume. | ||
| 141 | */ | ||
| 142 | ✗ | Scalar pressure(int phaseIdx = 0) const | |
| 143 | 327200 | { return fluidState_.pressure(0); } | |
| 144 | |||
| 145 | /*! | ||
| 146 | * \brief Returns the saturation. | ||
| 147 | */ | ||
| 148 | ✗ | Scalar saturation(int phaseIdx = 0) const | |
| 149 | ✗ | { return 1.0; } | |
| 150 | |||
| 151 | /*! | ||
| 152 | * \brief Return the mass density \f$\mathrm{[kg/m^3]}\f$ of a given phase within the | ||
| 153 | * control volume. | ||
| 154 | */ | ||
| 155 | ✗ | Scalar density(int phaseIdx = 0) const | |
| 156 | 328719616 | { return fluidState_.density(0); } | |
| 157 | |||
| 158 | /*! | ||
| 159 | * \brief Return temperature \f$\mathrm{[K]}\f$ inside the sub-control volume. | ||
| 160 | * | ||
| 161 | * Note that we assume thermodynamic equilibrium, i.e. the | ||
| 162 | * temperatures of the rock matrix and of all fluid phases are | ||
| 163 | * identical. | ||
| 164 | */ | ||
| 165 | Scalar temperature() const | ||
| 166 |
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15769600 | { return fluidState_.temperature(); } |
| 167 | |||
| 168 | /*! | ||
| 169 | * \brief Return the effective dynamic viscosity \f$\mathrm{[Pa s]}\f$ of the fluid within the | ||
| 170 | * control volume. | ||
| 171 | */ | ||
| 172 | Scalar effectiveViscosity() const | ||
| 173 | { return viscosity(); } | ||
| 174 | |||
| 175 | /*! | ||
| 176 | * \brief Return the dynamic viscosity \f$\mathrm{[Pa s]}\f$ of the fluid within the | ||
| 177 | * control volume. | ||
| 178 | */ | ||
| 179 | ✗ | Scalar viscosity(int phaseIdx = 0) const | |
| 180 | 115186464 | { return fluidState_.viscosity(0); } | |
| 181 | |||
| 182 | /*! | ||
| 183 | * \brief Returns the mass fraction of a component in the phase \f$\mathrm{[-]}\f$ | ||
| 184 | * | ||
| 185 | * \param phaseIdx the index of the phase | ||
| 186 | * \param compIdx the index of the component | ||
| 187 | */ | ||
| 188 | ✗ | Scalar massFraction(int phaseIdx, int compIdx) const | |
| 189 | { | ||
| 190 |
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55322712 | return fluidState_.massFraction(0, compIdx); |
| 191 | } | ||
| 192 | |||
| 193 | /*! | ||
| 194 | * \brief Returns the mass fraction of a component in the phase \f$\mathrm{[-]}\f$ | ||
| 195 | * | ||
| 196 | * \param compIdx the index of the component | ||
| 197 | */ | ||
| 198 | Scalar massFraction(int compIdx) const | ||
| 199 | { | ||
| 200 |
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225800 | return fluidState_.massFraction(0, compIdx); |
| 201 | } | ||
| 202 | |||
| 203 | /*! | ||
| 204 | * \brief Returns the mole fraction of a component in the phase \f$\mathrm{[-]}\f$ | ||
| 205 | * | ||
| 206 | * \param phaseIdx the index of the phase | ||
| 207 | * \param compIdx the index of the component | ||
| 208 | */ | ||
| 209 | ✗ | Scalar moleFraction(int phaseIdx, int compIdx) const | |
| 210 | { | ||
| 211 | 30289920 | return fluidState_.moleFraction(0, compIdx); | |
| 212 | } | ||
| 213 | |||
| 214 | /*! | ||
| 215 | * \brief Returns the mole fraction of a component in the phase \f$\mathrm{[-]}\f$ | ||
| 216 | * | ||
| 217 | * \param compIdx the index of the component | ||
| 218 | */ | ||
| 219 | Scalar moleFraction(int compIdx) const | ||
| 220 | { | ||
| 221 |
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67769696 | return fluidState_.moleFraction(0, compIdx); |
| 222 | } | ||
| 223 | |||
| 224 | /*! | ||
| 225 | * \brief Returns the mass density of a given phase \f$\mathrm{[kg/m^3]}\f$ | ||
| 226 | */ | ||
| 227 | ✗ | Scalar molarDensity(int phaseIdx = 0) const | |
| 228 | { | ||
| 229 | 66300896 | return fluidState_.molarDensity(0); | |
| 230 | } | ||
| 231 | |||
| 232 | /*! | ||
| 233 | * \brief Returns the molar mass of a given component. | ||
| 234 | * | ||
| 235 | * \param compIdx the index of the component | ||
| 236 | */ | ||
| 237 | Scalar molarMass(int compIdx) const | ||
| 238 | { | ||
| 239 | return FluidSystem::molarMass(compIdx); | ||
| 240 | } | ||
| 241 | |||
| 242 | /*! | ||
| 243 | * \brief Returns the average molar mass \f$\mathrm{[kg/mol]}\f$ of the fluid phase. | ||
| 244 | * | ||
| 245 | * \param phaseIdx The phase index | ||
| 246 | */ | ||
| 247 | Scalar averageMolarMass(const int phaseIdx = 0) const | ||
| 248 | 3786240 | { return fluidState_.averageMolarMass(phaseIdx); } | |
| 249 | |||
| 250 | /*! | ||
| 251 | * \brief Returns the binary diffusion coefficients for a phase in \f$[m^2/s]\f$. | ||
| 252 | */ | ||
| 253 | ✗ | Scalar diffusionCoefficient(int phaseIdx, int compIIdx, int compJIdx) const | |
| 254 | 107500 | { return diffCoefficient_(0, compIIdx, compJIdx); } | |
| 255 | |||
| 256 | /*! | ||
| 257 | * \brief Returns the effective diffusion coefficients for a phase in \f$[m^2/s]\f$. | ||
| 258 | */ | ||
| 259 | ✗ | Scalar effectiveDiffusionCoefficient(int phaseIdx, int compIIdx, int compJIdx) const | |
| 260 |
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26919520 | { return diffusionCoefficient(0, compIIdx, compJIdx); } |
| 261 | |||
| 262 | /*! | ||
| 263 | * \brief Return the fluid state of the control volume. | ||
| 264 | */ | ||
| 265 | const FluidState& fluidState() const | ||
| 266 |
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15790100 | { return fluidState_; } |
| 267 | |||
| 268 | protected: | ||
| 269 | FluidState fluidState_; | ||
| 270 | // Binary diffusion coefficient | ||
| 271 | DiffusionCoefficients diffCoefficient_; | ||
| 272 | }; | ||
| 273 | |||
| 274 | } // end namespace Dumux | ||
| 275 | |||
| 276 | #endif // DUMUX_NAVIERSTOKES_MOMENTUM_VOLUME_VARIABLES_HH | ||
| 277 |