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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 Binarycoefficients | ||
10 | * \brief Binary coefficients for water and air. | ||
11 | */ | ||
12 | #ifndef DUMUX_BINARY_COEFF_H2O_AIR_HH | ||
13 | #define DUMUX_BINARY_COEFF_H2O_AIR_HH | ||
14 | |||
15 | #include <cmath> | ||
16 | |||
17 | namespace Dumux::BinaryCoeff { | ||
18 | |||
19 | /*! | ||
20 | * \ingroup Binarycoefficients | ||
21 | * \brief Binary coefficients for water and air. | ||
22 | */ | ||
23 | class H2O_Air | ||
24 | { | ||
25 | public: | ||
26 | /*! | ||
27 | * \brief Henry coefficient \f$\mathrm{[Pa]}\f$ for air in liquid water. | ||
28 | * \param temperature the temperature \f$\mathrm{[K]}\f$ | ||
29 | * | ||
30 | * Henry coefficient See: | ||
31 | * Stefan Finsterle (1993, page 33 Formula (2.9)) \cite finsterle1993 <BR> | ||
32 | * (fitted to data from Tchobanoglous & Schroeder, 1985 \cite tchobanoglous1985 ) | ||
33 | */ | ||
34 | template <class Scalar> | ||
35 | 12933896 | static Scalar henry(Scalar temperature) | |
36 | { | ||
37 | using std::exp; | ||
38 | 12933896 | Scalar r = (0.8942+1.47*exp(-0.04394*(temperature-273.15)))*1.E-10; | |
39 | |||
40 | 12933896 | return 1./r; | |
41 | } | ||
42 | |||
43 | /*! | ||
44 | * \brief Binary diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular water and air | ||
45 | * | ||
46 | * \param temperature the temperature \f$\mathrm{[K]}\f$ | ||
47 | * \param pressure the phase pressure \f$\mathrm{[Pa]}\f$ | ||
48 | * Vargaftik: Tables on the thermophysical properties of liquids and gases. | ||
49 | * John Wiley & Sons, New York, 1975. \cite vargaftik1975 <BR> | ||
50 | * Walker, Sabey, Hampton: Studies of heat transfer and water migration in soils. | ||
51 | * Dep. of Agricultural and Chemical Engineering, Colorado State University, | ||
52 | * Fort Collins, 1981. \cite walker1981 | ||
53 | */ | ||
54 | template <class Scalar> | ||
55 | 52791195 | static Scalar gasDiffCoeff(Scalar temperature, Scalar pressure) | |
56 | { | ||
57 | 52791196 | const Scalar Theta=1.8; | |
58 | 52791196 | const Scalar Daw=2.13e-5; /* reference value */ | |
59 | 52791196 | const Scalar pg0=1.e5; /* reference pressure */ | |
60 |
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52791196 | const Scalar T0=273.15; /* reference temperature */ |
61 | Scalar Dgaw; | ||
62 | |||
63 | using std::pow; | ||
64 |
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52791195 | Dgaw=Daw*(pg0/pressure)*pow((temperature/T0),Theta); |
65 | |||
66 | return Dgaw; | ||
67 | } | ||
68 | |||
69 | /*! | ||
70 | * Lacking better data on water-air diffusion in liquids, we use at the | ||
71 | * moment the diffusion coefficient of the air's main component nitrogen!! | ||
72 | * \brief Diffusion coefficient \f$\mathrm{[m^2/s]}\f$ for molecular nitrogen in liquid water. | ||
73 | * | ||
74 | * \param temperature the temperature \f$\mathrm{[K]}\f$ | ||
75 | * \param pressure the phase pressure \f$\mathrm{[Pa]}\f$ | ||
76 | * | ||
77 | * The empirical equations for estimating the diffusion coefficient in | ||
78 | * infinite solution which are presented in Reid, 1987 all show a | ||
79 | * linear dependency on temperature. We thus simply scale the | ||
80 | * experimentally obtained diffusion coefficient of Ferrell and | ||
81 | * Himmelblau by the temperature. | ||
82 | * | ||
83 | * See: | ||
84 | * R. Reid et al. (1987, pp. 599) \cite reid1987 <BR> | ||
85 | * R. Ferrell, D. Himmelblau (1967, pp. 111-115) \cite ferrell1967 | ||
86 | */ | ||
87 | template <class Scalar> | ||
88 | 32190517 | static Scalar liquidDiffCoeff(Scalar temperature, Scalar pressure) | |
89 | { | ||
90 | 32190518 | const Scalar Texp = 273.15 + 25; // [K] | |
91 |
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32190518 | const Scalar Dexp = 2.01e-9; // [m^2/s] |
92 |
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32190517 | return Dexp * temperature/Texp; |
93 | } | ||
94 | }; | ||
95 | |||
96 | } // end namespace Dumux::BinaryCoeff | ||
97 | |||
98 | #endif | ||
99 |