机构:
Aix Marseille Univ, CNRS, UMR 7343, IUSTI, 5 Rue Enrico Fermi, F-13453 Marseille 13, FranceAix Marseille Univ, CNRS, UMR 7343, IUSTI, 5 Rue Enrico Fermi, F-13453 Marseille 13, France
Le Metayer, Olivier
[1
]
Saurel, Richard
论文数: 0引用数: 0
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机构:
Aix Marseille Univ, CNRS, UMR 7340 M2P2, Cent Marseille, 38 Rue Joliot Curie, F-13451 Marseille, France
RS2N, 371 Chemin Gaumin, F-83640 St Zacharie, France
Univ Inst France, Paris, FranceAix Marseille Univ, CNRS, UMR 7343, IUSTI, 5 Rue Enrico Fermi, F-13453 Marseille 13, France
Saurel, Richard
[2
,3
,4
]
机构:
[1] Aix Marseille Univ, CNRS, UMR 7343, IUSTI, 5 Rue Enrico Fermi, F-13453 Marseille 13, France
[2] Aix Marseille Univ, CNRS, UMR 7340 M2P2, Cent Marseille, 38 Rue Joliot Curie, F-13451 Marseille, France
[3] RS2N, 371 Chemin Gaumin, F-83640 St Zacharie, France
Hyperbolic two-phase flow models have shown excellent ability for the resolution of a wide range of applications ranging from interfacial flows to fluid mixtures with several velocities. These models account for waves propagation (acoustic and convective) and consist in hyperbolic systems of partial differential equations. In this context, each phase is compressible and needs an appropriate convex equation of state (EOS). The EOS must be simple enough for intensive computations as well as boundary conditions treatment. It must also be accurate, this being challenging with respect to simplicity. In the present approach, each fluid is governed by a novel EOS named "Noble Abel stiffened gas," this formulation being a significant improvement of the popular "Stiffened Gas (SG)" EOS. It is a combination of the so-called "Noble-Abel" and " stiffened gas" equations of state that adds repulsive effects to the SG formulation. The determination of the various thermodynamic functions and associated coefficients is the aim of this article. We first use thermodynamic considerations to determine the different state functions such as the specific internal energy, enthalpy, and entropy. Then we propose to determine the associated coefficients for a liquid in the presence of its vapor. The EOS parameters are determined from experimental saturation curves. Some examples of liquid-vapor fluids are examined and associated parameters are computed with the help of the present method. Comparisons between analytical and experimental saturation curves show very good agreement for wide ranges of temperature for both liquid and vapor. Published by AIP Publishing.