2011
DOI: 10.1016/j.matcom.2010.12.016
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Finite volume approximation of a diffusion–dissolution model and application to nuclear waste storage

Abstract: The study of two phase flow in porous media under high capillary pressures, in the case where one phase is incompressible and the other phase is gaseous, shows complex phenomena. We present in this paper a numerical approximation method, based on a two pressures formulation in the case where both phases are miscible, which is shown to also handle the limit case of immiscible phases. The space discretization is performed using a finite volume method, which can handle general grids. The efficiency of the formula… Show more

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Cited by 30 publications
(34 citation statements)
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References 10 publications
(18 reference statements)
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“…Alternately, we also consider the case of Richards' equation, which can be obtained from (1) in two ways. One can replace (1a) by u(x, t) =ū(x) for (x, t) ∈ Ω × (0, T ),…”
Section: (φ(X)s(x P(x T))∂ T ϕ(X T) + K 2 (X S(x P(x T)))λ(x)(∇mentioning
confidence: 99%
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“…Alternately, we also consider the case of Richards' equation, which can be obtained from (1) in two ways. One can replace (1a) by u(x, t) =ū(x) for (x, t) ∈ Ω × (0, T ),…”
Section: (φ(X)s(x P(x T))∂ T ϕ(X T) + K 2 (X S(x P(x T)))λ(x)(∇mentioning
confidence: 99%
“…The existence of a weak solution to Problem (1), under various hypotheses, is studied in [2,8,12,20] for example. Some mathematical results of convergence have been obtained for several approximations of this problem.…”
Section: (φ(X)s(x P(x T))∂ T ϕ(X T) + K 2 (X S(x P(x T)))λ(x)(∇mentioning
confidence: 99%
“…From remarks 1 and 2, a one parameter family of independent on x Robin coefficients L, M i , i = a, w, N can be obtained using L > 0 as a real parameter and setting (17), (19), (22). We deduce that independent on x Robin coefficients can be competitive for this test case and also that our computation almost reaches the optimal number of iterations of this one parameter family.…”
Section: Andra Test Casementioning
confidence: 61%
“…Following [19,20], our choice of the liquid gas Darcy flow formulation uses the pressures p g , p of both phases, the vector f = (f i ) i∈C of the component fugacities and the temperature, denoted by T pm in the porous medium, as primary unknowns.…”
Section: Nonisothermal Compositional Darcy Flow In the Porous Mediummentioning
confidence: 99%
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