High pressure solid-fluid and vapour-liquid equilibria in the system (methane + tetracosane)

• Published in: Fluid phase equilibria 1997-01, Vol.127 (1), p.129-146
• Main Authors: Flöter, E., de Loos, Th.W., de Swaan Arons, J.
• Format: Article
• Language: English
• Subjects: Asymmetric n-alkane mixtures; Chemistry; Exact sciences and technology; Experimental data; General and physical chemistry; High pressure; Others (including liquid-liquid-vapor equilibria); Phase equilibria; Solid-fluid equilibria; Vapour-liquid equilibria; Wax formation
• ISSN: 0378-3812; 1879-0224
• DOI: 10.1016/S0378-3812(96)03157-3

Experimental vapour-liquid, solid-fluid, and solid-liquid-vapour equilibrium data of the binary system (methane + tetracosane) in the temperature range 315–450 K and for pressures up to 200 MPa are presented. The experiments were carried out for various mixtures with compositions ranging from almost pure methane to pure tetracosane. It was found that the (solid α-to-solidβ) transition of pure tetracosane has hardly any influence on the shape of the (solid + fluid/fluid) boundary curves and the three-phase equilibrium curve (solid tetracosane + liquid + vapour) of the binary system. The second critical endpoint of the three-phase curve (s C24 + 1 = g), where solid tetracosane is in equilibrium with a critical fluid phase was located at a temperature of T = (322.60 ± 0.25)K, a pressure of p = (104.7 ± 0.4)MPa, and a mole fraction of tetracosane in the critical fluid phase of x C24 = (0.041 ± 0.003).