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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 FluidSystems | ||
| 10 | * \brief @copybrief Dumux::FluidSystems::OnePGas | ||
| 11 | */ | ||
| 12 | #ifndef DUMUX_GAS_PHASE_HH | ||
| 13 | #define DUMUX_GAS_PHASE_HH | ||
| 14 | |||
| 15 | #include <cassert> | ||
| 16 | #include <limits> | ||
| 17 | |||
| 18 | #include <dune/common/exceptions.hh> | ||
| 19 | |||
| 20 | #include <dumux/material/fluidsystems/base.hh> | ||
| 21 | #include <dumux/material/components/componenttraits.hh> | ||
| 22 | #include <dumux/io/name.hh> | ||
| 23 | |||
| 24 | namespace Dumux { | ||
| 25 | namespace FluidSystems { | ||
| 26 | |||
| 27 | /*! | ||
| 28 | * \ingroup FluidSystems | ||
| 29 | * \brief A gaseous phase consisting of a single component | ||
| 30 | */ | ||
| 31 | template <class Scalar, class ComponentT> | ||
| 32 | class OnePGas | ||
| 33 | : public Base<Scalar, OnePGas<Scalar, ComponentT> > | ||
| 34 | { | ||
| 35 | using ThisType = OnePGas<Scalar, ComponentT>; | ||
| 36 | |||
| 37 | static_assert(ComponentTraits<ComponentT>::hasGasState, "The component does not implement a gas state!"); | ||
| 38 | |||
| 39 | public: | ||
| 40 | using Component = ComponentT; | ||
| 41 | using ParameterCache = NullParameterCache; | ||
| 42 | |||
| 43 | static constexpr int numPhases = 1; //!< Number of phases in the fluid system | ||
| 44 | static constexpr int numComponents = 1; //!< Number of components in the fluid system | ||
| 45 | |||
| 46 | static constexpr int phase0Idx = 0; //!< index of the only phase | ||
| 47 | static constexpr int comp0Idx = 0; //!< index of the only component | ||
| 48 | |||
| 49 | /*! | ||
| 50 | * \brief Initialize the fluid system's static parameters generically | ||
| 51 | */ | ||
| 52 | static void init() | ||
| 53 | { } | ||
| 54 | |||
| 55 | /**************************************** | ||
| 56 | * Fluid phase related static parameters | ||
| 57 | ****************************************/ | ||
| 58 | /*! | ||
| 59 | * \brief Return the human readable name of a fluid phase | ||
| 60 | * | ||
| 61 | * \param phaseIdx The index of the fluid phase to consider | ||
| 62 | */ | ||
| 63 | ✗ | static std::string phaseName(int phaseIdx = 0) | |
| 64 | 638 | { return IOName::gaseousPhase(); } | |
| 65 | |||
| 66 | /*! | ||
| 67 | * \brief A human readable name for the component. | ||
| 68 | * | ||
| 69 | * \param compIdx The index of the component to consider | ||
| 70 | */ | ||
| 71 | ✗ | static std::string componentName(int compIdx = 0) | |
| 72 |
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1 | { return Component::name(); } |
| 73 | |||
| 74 | /*! | ||
| 75 | * \brief A human readable name for the component. | ||
| 76 | */ | ||
| 77 | static std::string name() | ||
| 78 | 4 | { return Component::name(); } | |
| 79 | |||
| 80 | /*! | ||
| 81 | * \brief There is only one phase, so not mass transfer between phases can occur | ||
| 82 | */ | ||
| 83 | static constexpr bool isMiscible() | ||
| 84 | { return false; } | ||
| 85 | |||
| 86 | /*! | ||
| 87 | * \brief Returns whether the fluid is gaseous | ||
| 88 | */ | ||
| 89 | ✗ | static constexpr bool isGas(int phaseIdx = 0) | |
| 90 | ✗ | { return true; } | |
| 91 | |||
| 92 | /*! | ||
| 93 | * \brief Returns true if and only if a fluid phase is assumed to | ||
| 94 | * be an ideal mixture. | ||
| 95 | * | ||
| 96 | * We define an ideal mixture as a fluid phase where the fugacity | ||
| 97 | * coefficients of all components times the pressure of the phase | ||
| 98 | * are independent on the fluid composition. This assumption is true | ||
| 99 | * if only a single component is involved. If you are unsure what | ||
| 100 | * this function should return, it is safe to return false. The | ||
| 101 | * only damage done will be (slightly) increased computation times | ||
| 102 | * in some cases. | ||
| 103 | * | ||
| 104 | * \param phaseIdx The index of the fluid phase to consider | ||
| 105 | */ | ||
| 106 | ✗ | static constexpr bool isIdealMixture(int phaseIdx = 0) | |
| 107 | ✗ | { return true; } | |
| 108 | |||
| 109 | /*! | ||
| 110 | * \brief Returns true if the fluid is assumed to be compressible | ||
| 111 | */ | ||
| 112 | ✗ | static constexpr bool isCompressible(int phaseIdx = 0) | |
| 113 | ✗ | { return Component::gasIsCompressible(); } | |
| 114 | |||
| 115 | /*! | ||
| 116 | * \brief Returns true if the fluid is assumed to be an ideal gas | ||
| 117 | */ | ||
| 118 | ✗ | static constexpr bool isIdealGas(int phaseIdx = 0) | |
| 119 | ✗ | { return Component::gasIsIdeal(); } | |
| 120 | |||
| 121 | /*! | ||
| 122 | * \brief Returns true if and only if a fluid phase is assumed to | ||
| 123 | * have a constant viscosity. | ||
| 124 | * | ||
| 125 | * \param phaseIdx The index of the fluid phase to consider | ||
| 126 | */ | ||
| 127 | static constexpr bool viscosityIsConstant(int phaseIdx) | ||
| 128 | { return Component::gasViscosityIsConstant(); } | ||
| 129 | |||
| 130 | /*! | ||
| 131 | * \brief The mass in \f$\mathrm{[kg]}\f$ of one mole of the component. | ||
| 132 | */ | ||
| 133 | ✗ | static Scalar molarMass(int compIdx = 0) | |
| 134 | ✗ | { return Component::molarMass(); } | |
| 135 | |||
| 136 | /*! | ||
| 137 | * \brief Returns the critical temperature in \f$\mathrm{[K]}\f$ of the component | ||
| 138 | */ | ||
| 139 | static Scalar criticalTemperature(int compIdx = 0) | ||
| 140 | { return Component::criticalTemperature(); } | ||
| 141 | |||
| 142 | /*! | ||
| 143 | * \brief Returns the critical pressure in \f$\mathrm{[Pa]}\f$ of the component | ||
| 144 | */ | ||
| 145 | static Scalar criticalPressure(int compIdx = 0) | ||
| 146 | { return Component::criticalPressure(); } | ||
| 147 | |||
| 148 | /*! | ||
| 149 | * \brief Returns the temperature in \f$\mathrm{[K]}\f$ at the component's triple point. | ||
| 150 | */ | ||
| 151 | static Scalar tripleTemperature(int compIdx = 0) | ||
| 152 | { return Component::tripleTemperature(); } | ||
| 153 | |||
| 154 | /*! | ||
| 155 | * \brief Returns the pressure in \f$\mathrm{[Pa]}\f$ at the component's triple point. | ||
| 156 | */ | ||
| 157 | static Scalar triplePressure(int compIdx = 0) | ||
| 158 | { return Component::triplePressure(); } | ||
| 159 | |||
| 160 | /*! | ||
| 161 | * \brief The vapor pressure in \f$\mathrm{[Pa]}\f$ of the component at a given | ||
| 162 | * temperature. | ||
| 163 | * \param T temperature \f$\mathrm{[K]}\f$ | ||
| 164 | */ | ||
| 165 | static Scalar vaporPressure(Scalar T) | ||
| 166 | { return Component::vaporPressure(T); } | ||
| 167 | |||
| 168 | /*! | ||
| 169 | * \brief The density \f$\mathrm{[kg/m^3]}\f$ of the component at a given pressure and temperature. | ||
| 170 | * \param temperature The given temperature \f$\mathrm{[K]}\f$ | ||
| 171 | * \param pressure The given pressure \f$\mathrm{[Pa]}\f$ | ||
| 172 | */ | ||
| 173 | static Scalar density(Scalar temperature, Scalar pressure) | ||
| 174 | 19975576 | { return Component::gasDensity(temperature, pressure); } | |
| 175 | |||
| 176 | using Base<Scalar, ThisType>::density; | ||
| 177 | //! \copydoc Base<Scalar,ThisType>::density(const FluidState&,int) | ||
| 178 | template <class FluidState> | ||
| 179 | 1 | static Scalar density(const FluidState &fluidState, | |
| 180 | const int phaseIdx) | ||
| 181 | { | ||
| 182 | return density(fluidState.temperature(phaseIdx), | ||
| 183 | 31 | fluidState.pressure(phaseIdx)); | |
| 184 | } | ||
| 185 | |||
| 186 | /*! | ||
| 187 | * \brief The molar density \f$\rho_{mol,\alpha}\f$ | ||
| 188 | * of a fluid phase \f$\alpha\f$ in \f$\mathrm{[mol/m^3]}\f$ | ||
| 189 | * | ||
| 190 | * The molar density is defined by the | ||
| 191 | * mass density \f$\rho_\alpha\f$ and the component molar mass \f$M_\alpha\f$: | ||
| 192 | * | ||
| 193 | * \f[\rho_{mol,\alpha} = \frac{\rho_\alpha}{M_\alpha} \;.\f] | ||
| 194 | * \param temperature The temperature at which to evaluate the molar density | ||
| 195 | * \param pressure The pressure at which to evaluate the molar density | ||
| 196 | */ | ||
| 197 | static Scalar molarDensity(Scalar temperature, Scalar pressure) | ||
| 198 | 8 | { return Component::gasMolarDensity(temperature, pressure); } | |
| 199 | |||
| 200 | using Base<Scalar, ThisType>::molarDensity; | ||
| 201 | //! \copydoc Base<Scalar,ThisType>::molarDensity(const FluidState&,int) | ||
| 202 | template <class FluidState> | ||
| 203 | 1 | static Scalar molarDensity(const FluidState &fluidState, | |
| 204 | const int phaseIdx) | ||
| 205 | { | ||
| 206 | return molarDensity(fluidState.temperature(phaseIdx), | ||
| 207 | 1 | fluidState.pressure(phaseIdx)); | |
| 208 | } | ||
| 209 | |||
| 210 | /*! | ||
| 211 | * \brief The pressure \f$\mathrm{[Pa]}\f$ of the component at a given density and temperature. | ||
| 212 | * \param temperature The given temperature \f$\mathrm{[K]}\f$ | ||
| 213 | * \param density The given density \f$\mathrm{[kg/m^3]}\f$ | ||
| 214 | */ | ||
| 215 | static Scalar pressure(Scalar temperature, Scalar density) | ||
| 216 | { return Component::gasPressure(temperature, density); } | ||
| 217 | |||
| 218 | /*! | ||
| 219 | * \brief Specific enthalpy \f$\mathrm{[J/kg]}\f$ of the pure component as a gas. | ||
| 220 | * \param temperature The given temperature \f$\mathrm{[K]}\f$ | ||
| 221 | * \param pressure The given pressure \f$\mathrm{[Pa]}\f$ | ||
| 222 | */ | ||
| 223 | ✗ | static const Scalar enthalpy(Scalar temperature, Scalar pressure) | |
| 224 | 8 | { return Component::gasEnthalpy(temperature, pressure); } | |
| 225 | |||
| 226 | using Base<Scalar, ThisType>::enthalpy; | ||
| 227 | //! \copydoc Base<Scalar,ThisType>::enthalpy(const FluidState&,int) | ||
| 228 | template <class FluidState> | ||
| 229 | 1 | static Scalar enthalpy(const FluidState &fluidState, | |
| 230 | const int phaseIdx) | ||
| 231 | { | ||
| 232 | return enthalpy(fluidState.temperature(phaseIdx), | ||
| 233 | 1 | fluidState.pressure(phaseIdx)); | |
| 234 | } | ||
| 235 | |||
| 236 | /*! | ||
| 237 | * \brief Specific internal energy \f$\mathrm{[J/kg]}\f$ of the pure component as a gas. | ||
| 238 | * \param temperature The given temperature \f$\mathrm{[K]}\f$ | ||
| 239 | * \param pressure The given pressure \f$\mathrm{[Pa]}\f$ | ||
| 240 | */ | ||
| 241 | static const Scalar internalEnergy(Scalar temperature, Scalar pressure) | ||
| 242 | { return Component::gasInternalEnergy(temperature, pressure); } | ||
| 243 | |||
| 244 | /*! | ||
| 245 | * \brief The dynamic viscosity \f$\mathrm{[Pa s]}\f$ of the pure component at a given pressure and temperature. | ||
| 246 | * \param temperature The given temperature \f$\mathrm{[K]}\f$ | ||
| 247 | * \param pressure The given pressure \f$\mathrm{[Pa]}\f$ | ||
| 248 | */ | ||
| 249 | static Scalar viscosity(Scalar temperature, Scalar pressure) | ||
| 250 | 5004857 | { return Component::gasViscosity(temperature, pressure); } | |
| 251 | |||
| 252 | using Base<Scalar, ThisType>::viscosity; | ||
| 253 | //! \copydoc Base<Scalar,ThisType>::viscosity(const FluidState&,int) | ||
| 254 | template <class FluidState> | ||
| 255 | 1 | static Scalar viscosity(const FluidState &fluidState, | |
| 256 | const int phaseIdx) | ||
| 257 | { | ||
| 258 | return viscosity(fluidState.temperature(phaseIdx), | ||
| 259 |
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16 | fluidState.pressure(phaseIdx)); |
| 260 | } | ||
| 261 | |||
| 262 | using Base<Scalar, ThisType>::fugacityCoefficient; | ||
| 263 | //! \copydoc Base<Scalar,ThisType>::fugacityCoefficient(const FluidState&,int,int) | ||
| 264 | template <class FluidState> | ||
| 265 | ✗ | static Scalar fugacityCoefficient(const FluidState &fluidState, | |
| 266 | int phaseIdx, | ||
| 267 | int compIdx) | ||
| 268 | { | ||
| 269 | ✗ | assert(0 <= phaseIdx && phaseIdx < numPhases); | |
| 270 | ✗ | assert(0 <= compIdx && compIdx < numComponents); | |
| 271 | |||
| 272 | if (phaseIdx == compIdx) | ||
| 273 | // We could calculate the real fugacity coefficient of | ||
| 274 | // the component in the fluid. Probably that's not worth | ||
| 275 | // the effort, since the fugacity coefficient of the other | ||
| 276 | // component is infinite anyway... | ||
| 277 | ✗ | return 1.0; | |
| 278 | return std::numeric_limits<Scalar>::infinity(); | ||
| 279 | } | ||
| 280 | |||
| 281 | using Base<Scalar, ThisType>::diffusionCoefficient; | ||
| 282 | //! \copydoc Base<Scalar,ThisType>::diffusionCoefficient(const FluidState&,int,int) | ||
| 283 | template <class FluidState> | ||
| 284 | 1 | static Scalar diffusionCoefficient(const FluidState &fluidState, | |
| 285 | int phaseIdx, | ||
| 286 | int compIdx) | ||
| 287 | { | ||
| 288 |
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11 | DUNE_THROW(Dune::InvalidStateException, "Not applicable: Diffusion coefficients"); |
| 289 | } | ||
| 290 | |||
| 291 | using Base<Scalar, ThisType>::binaryDiffusionCoefficient; | ||
| 292 | //! \copydoc Base<Scalar,ThisType>::binaryDiffusionCoefficient(const FluidState&,int,int,int) | ||
| 293 | template <class FluidState> | ||
| 294 | 1 | static Scalar binaryDiffusionCoefficient(const FluidState &fluidState, | |
| 295 | int phaseIdx, | ||
| 296 | int compIIdx, | ||
| 297 | int compJIdx) | ||
| 298 | |||
| 299 | { | ||
| 300 |
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11 | DUNE_THROW(Dune::InvalidStateException, "Not applicable: Binary diffusion coefficients"); |
| 301 | } | ||
| 302 | |||
| 303 | /*! | ||
| 304 | * \brief Thermal conductivity of the fluid \f$\mathrm{[W/(m K)]}\f$. | ||
| 305 | * \param temperature The given temperature \f$\mathrm{[K]}\f$ | ||
| 306 | * \param pressure The given pressure \f$\mathrm{[Pa]}\f$ | ||
| 307 | */ | ||
| 308 | ✗ | static Scalar thermalConductivity(Scalar temperature, Scalar pressure) | |
| 309 | 68786564 | { return Component::gasThermalConductivity(temperature, pressure); } | |
| 310 | |||
| 311 | using Base<Scalar, ThisType>::thermalConductivity; | ||
| 312 | //! \copydoc Base<Scalar,ThisType>::thermalConductivity(const FluidState&,int) | ||
| 313 | template <class FluidState> | ||
| 314 | 1 | static Scalar thermalConductivity(const FluidState &fluidState, | |
| 315 | const int phaseIdx) | ||
| 316 | { | ||
| 317 | return thermalConductivity(fluidState.temperature(phaseIdx), | ||
| 318 | 68623261 | fluidState.pressure(phaseIdx)); | |
| 319 | } | ||
| 320 | |||
| 321 | /*! | ||
| 322 | * \brief Specific isobaric heat capacity of the fluid \f$\mathrm{[J/(kg K)]}\f$. | ||
| 323 | * \param temperature The given temperature \f$\mathrm{[K]}\f$ | ||
| 324 | * \param pressure The given pressure \f$\mathrm{[Pa]}\f$ | ||
| 325 | */ | ||
| 326 | ✗ | static Scalar heatCapacity(Scalar temperature, Scalar pressure) | |
| 327 | 24863940 | { return Component::gasHeatCapacity(temperature, pressure); } | |
| 328 | |||
| 329 | using Base<Scalar, ThisType>::heatCapacity; | ||
| 330 | //! \copydoc Base<Scalar,ThisType>::heatCapacity(const FluidState&,int) | ||
| 331 | template <class FluidState> | ||
| 332 | 1 | static Scalar heatCapacity(const FluidState &fluidState, | |
| 333 | const int phaseIdx) | ||
| 334 | { | ||
| 335 | return heatCapacity(fluidState.temperature(phaseIdx), | ||
| 336 | 24863933 | fluidState.pressure(phaseIdx)); | |
| 337 | } | ||
| 338 | }; | ||
| 339 | |||
| 340 | } // namespace FluidSystems | ||
| 341 | } // namespace | ||
| 342 | |||
| 343 | #endif | ||
| 344 |