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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 Components | ||
| 10 | * \brief A simple implementation of Trichloroethene (TCE), a DNAPL. | ||
| 11 | */ | ||
| 12 | #ifndef DUMUX_TRICHLOROETHENE_HH | ||
| 13 | #define DUMUX_TRICHLOROETHENE_HH | ||
| 14 | |||
| 15 | #include <dumux/material/idealgas.hh> | ||
| 16 | |||
| 17 | #include <dumux/material/components/base.hh> | ||
| 18 | #include <dumux/material/components/liquid.hh> | ||
| 19 | #include <dumux/material/components/gas.hh> | ||
| 20 | |||
| 21 | namespace Dumux::Components { | ||
| 22 | |||
| 23 | /*! | ||
| 24 | * \ingroup Components | ||
| 25 | * \brief A simple implementation of TCE as exemplary component for a dense NAPL. | ||
| 26 | * | ||
| 27 | * \tparam Scalar The type used for scalar values | ||
| 28 | */ | ||
| 29 | template <class Scalar> | ||
| 30 | class Trichloroethene | ||
| 31 | : public Components::Base<Scalar, Trichloroethene<Scalar> > | ||
| 32 | , public Components::Liquid<Scalar, Trichloroethene<Scalar> > | ||
| 33 | , public Components::Gas<Scalar, Trichloroethene<Scalar> > | ||
| 34 | { | ||
| 35 | typedef Dumux::IdealGas<Scalar> IdealGas; | ||
| 36 | |||
| 37 | public: | ||
| 38 | /*! | ||
| 39 | * \brief A human readable name for the dense NAPL TCE. | ||
| 40 | */ | ||
| 41 |
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4 | static std::string name() |
| 42 |
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4 | { return "Trichloroethene"; } |
| 43 | |||
| 44 | /*! | ||
| 45 | * \brief The molar mass in \f$\mathrm{[kg/mol]}\f$ of TCE. | ||
| 46 | */ | ||
| 47 | static constexpr Scalar molarMass() | ||
| 48 | { | ||
| 49 | return 131.39e-3; // [kg/mol] | ||
| 50 | } | ||
| 51 | |||
| 52 | /*! | ||
| 53 | * \brief Returns the critical temperature \f$\mathrm{[K]}\f$ of TCE. | ||
| 54 | */ | ||
| 55 | static Scalar criticalTemperature() | ||
| 56 | { | ||
| 57 | DUNE_THROW(Dune::NotImplemented, "criticalTemperature for TCE"); | ||
| 58 | } | ||
| 59 | |||
| 60 | /*! | ||
| 61 | * \brief Returns the critical pressure \f$\mathrm{[Pa]}\f$ of TCE. | ||
| 62 | */ | ||
| 63 | static Scalar criticalPressure() | ||
| 64 | { | ||
| 65 | DUNE_THROW(Dune::NotImplemented, "criticalPressure for TCE"); | ||
| 66 | } | ||
| 67 | |||
| 68 | /*! | ||
| 69 | * \brief Returns the temperature \f$\mathrm{[K]}\f$ at TCE's triple point. | ||
| 70 | */ | ||
| 71 | static Scalar tripleTemperature() | ||
| 72 | { | ||
| 73 | DUNE_THROW(Dune::NotImplemented, "tripleTemperature for TCE"); | ||
| 74 | } | ||
| 75 | |||
| 76 | /*! | ||
| 77 | * \brief Returns the pressure \f$\mathrm{[Pa]}\f$ at TCE's triple point. | ||
| 78 | */ | ||
| 79 | static Scalar triplePressure() | ||
| 80 | { | ||
| 81 | DUNE_THROW(Dune::NotImplemented, "triplePressure for TCE"); | ||
| 82 | } | ||
| 83 | |||
| 84 | /*! | ||
| 85 | * \brief The vapor pressure in \f$\mathrm{[Pa]}\f$ of pure TCE | ||
| 86 | * at a given temperature. | ||
| 87 | * | ||
| 88 | * \param T temperature of component in \f$\mathrm{[K]}\f$ | ||
| 89 | */ | ||
| 90 | static Scalar vaporPressure(Scalar T) | ||
| 91 | { | ||
| 92 | return 3900; // [Pa] (at 20C) | ||
| 93 | } | ||
| 94 | |||
| 95 | /*! | ||
| 96 | * \brief Returns true if the gas phase is assumed to be compressible | ||
| 97 | */ | ||
| 98 | static constexpr bool gasIsCompressible() | ||
| 99 | { return true; } | ||
| 100 | |||
| 101 | /*! | ||
| 102 | * \brief Returns true if the liquid phase is assumed to be compressible | ||
| 103 | */ | ||
| 104 | static constexpr bool liquidIsCompressible() | ||
| 105 | { return false; } | ||
| 106 | |||
| 107 | /*! | ||
| 108 | * \brief Returns true if the liquid phase viscostiy is constant | ||
| 109 | */ | ||
| 110 | static constexpr bool liquidViscosityIsConstant() | ||
| 111 | { return true; } | ||
| 112 | |||
| 113 | /*! | ||
| 114 | * \brief The density of steam at a given pressure and temperature \f$\mathrm{[kg/m^3]}\f$. | ||
| 115 | * | ||
| 116 | * \param temperature temperature of component in \f$\mathrm{[K]}\f$ | ||
| 117 | * \param pressure pressure of component in \f$\mathrm{[Pa]}\f$ | ||
| 118 | */ | ||
| 119 |
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113 | static Scalar gasDensity(Scalar temperature, Scalar pressure) |
| 120 | { | ||
| 121 |
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113 | return IdealGas::density(molarMass(), |
| 122 | temperature, | ||
| 123 | pressure); | ||
| 124 | } | ||
| 125 | |||
| 126 | /*! | ||
| 127 | * \brief The molar density of steam in \f$\mathrm{[mol/m^3]}\f$ at a given pressure and temperature. | ||
| 128 | * | ||
| 129 | * \param temperature temperature of component in \f$\mathrm{[K]}\f$ | ||
| 130 | * \param pressure pressure of component in \f$\mathrm{[Pa]}\f$ | ||
| 131 | * | ||
| 132 | */ | ||
| 133 | static Scalar gasMolarDensity(Scalar temperature, Scalar pressure) | ||
| 134 | { return IdealGas::molarDensity(temperature, pressure); } | ||
| 135 | |||
| 136 | /*! | ||
| 137 | * \brief Returns true if the gas phase is assumed to be ideal | ||
| 138 | */ | ||
| 139 | static constexpr bool gasIsIdeal() | ||
| 140 | { return true; } | ||
| 141 | |||
| 142 | /*! | ||
| 143 | * \brief The density of pure TCE at a given pressure and temperature \f$\mathrm{[kg/m^3]}\f$. | ||
| 144 | * | ||
| 145 | * \param temperature temperature of component in \f$\mathrm{[K]}\f$ | ||
| 146 | * \param pressure pressure of component in \f$\mathrm{[Pa]}\f$ | ||
| 147 | */ | ||
| 148 | static Scalar liquidDensity(Scalar temperature, Scalar pressure) | ||
| 149 | { | ||
| 150 | return 1460.0; // [kg/m^3] | ||
| 151 | } | ||
| 152 | |||
| 153 | /*! | ||
| 154 | * \brief The molar density of pure TCE in \f$\mathrm{[mol/m^3]}\f$ at a given pressure and temperature. | ||
| 155 | * | ||
| 156 | * \param temperature temperature of component in \f$\mathrm{[K]}\f$ | ||
| 157 | * \param pressure pressure of component in \f$\mathrm{[Pa]}\f$ | ||
| 158 | * | ||
| 159 | */ | ||
| 160 | static Scalar liquidMolarDensity(Scalar temperature, Scalar pressure) | ||
| 161 | { return liquidDensity(temperature, pressure)/molarMass(); } | ||
| 162 | |||
| 163 | /*! | ||
| 164 | * \brief The dynamic viscosity \f$\mathrm{[Pa*s]}\f$ of pure TCE. | ||
| 165 | * | ||
| 166 | * \param temperature temperature of component in \f$\mathrm{[K]}\f$ | ||
| 167 | * \param pressure pressure of component in \f$\mathrm{[Pa]}\f$ | ||
| 168 | */ | ||
| 169 | static Scalar liquidViscosity(Scalar temperature, Scalar pressure) | ||
| 170 | { | ||
| 171 | return 5.7e-4;// [Pa*s] | ||
| 172 | } | ||
| 173 | }; | ||
| 174 | |||
| 175 | } // end namespace Dumux::Components | ||
| 176 | |||
| 177 | #endif | ||
| 178 |