Liquid-Vapor Equilibrium in the System Uranium Hexafluoride-Hydrogen Fluoride

Roger L. Jarry; Fred D. Rosen; Charley F. Hale; Wallace Davis

doi:10.1021/j150510a011

Liquid-Vapor Equilibrium in the System Uranium Hexafluoride-Hydrogen Fluoride

The Journal of Physical Chemistry ◽

10.1021/j150510a011 ◽

1953 ◽

Vol 57 (9) ◽

pp. 905-909 ◽

Cited By ~ 9

Author(s):

Roger L. Jarry ◽

Fred D. Rosen ◽

Charley F. Hale ◽

Wallace Davis

Keyword(s):

Hydrogen Fluoride ◽

Uranium Hexafluoride ◽

Vapor Equilibrium ◽

Liquid Vapor

Download Full-text

Liquid-vapor equilibrium in systems with dilute solutions of metal fluorides in uranium hexafluoride

Soviet Atomic Energy ◽

10.1007/bf01132645 ◽

1976 ◽

Vol 41 (2) ◽

pp. 711-714

Author(s):

V. N. Prusakov ◽

V. K. Ezhov ◽

E. A. Efremov

Keyword(s):

Uranium Hexafluoride ◽

Dilute Solutions ◽

Metal Fluorides ◽

Vapor Equilibrium ◽

Liquid Vapor

Download Full-text

Liquid-vapor equilibrium in the system helium-methane

AIChE Journal ◽

10.1002/aic.690130335 ◽

1967 ◽

Vol 13 (3) ◽

pp. 593-599 ◽

Cited By ~ 21

Author(s):

C. K. Heck ◽

M. J. Hiza

Keyword(s):

Vapor Equilibrium ◽

Liquid Vapor

Download Full-text

EQUATIONS OF STATE FOR FLUIDS: THE LIQUID-VAPOR EQUILIBRIUM (LVE)

International Journal of Modern Physics B ◽

10.1142/s021797920804942x ◽

2008 ◽

Vol 22 (30) ◽

pp. 5335-5347 ◽

Cited By ~ 3

Author(s):

JIANXIANG TIAN ◽

YUANXING GUI

Keyword(s):

Experimental Data ◽

Equations Of State ◽

Packing Fraction ◽

Optimal Choice ◽

Critical Conditions ◽

Mechanics Model ◽

Vapor Equilibrium ◽

Pure Substances ◽

Compressibility Factors ◽

Liquid Vapor

Historically, the development of equations of state for fluids has almost invariably followed the lead of the van der Waals (vdW) equation which includes an attraction term and a repulsion term. In this paper, using a simple statistical mechanics model, we introduce a parameter σ as both the power and a coefficient of the packing fraction y which locates at the numerator of the vdW attraction term. Then nine equations of state are constructed to solve the critical conditions and the main thermodynamic properties of pure substances at liquid-vapor equilibrium. As a result, the correct critical compressibility factors of Nitrogen, Argon, Carbon dioxide, Ethene, Methane, Oxygen, Propene, Water and Hydrogen, are obtained with an optimal choice of parameter σ. Good predictions of these equations to the liquid-vapor equilibrium properties below critical temperature are reported and compared with experimental data.

Download Full-text