Title of article
Liquid–vapour and solid–fluid equilibria for the system methane + triacontane at high temperature and high pressure
Author/Authors
Machado، نويسنده , , J.J.B. and de Loos، نويسنده , , Th.W.، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2004
Pages
7
From page
261
To page
267
Abstract
In this work experimental vapour–liquid and solid–fluid equilibrium data are presented for 13 different compositions of the system methane + triacontane. This data cover the temperature range from 315 to 450 K, and pressures up to 200 MPa. The compositions studied range from almost pure methane to pure triacontane. On the basis of the primary experimental two-phase equilibrium results, the course of the three-phase curve (solid triacontane + liquid + vapour) was derived. The second critical endpoint of this curve, where solid triacontane is in equilibrium with a critical fluid phase (sC30 + (l = g)) was found at T = 340.73 ± 0.4 K, P = 128.55 ± 0.5 MPa and a mole fraction in the critical fluid phase of xC30 = 0.0275 ± 0.002.
Keywords
Solid–fluid equilibria , Methane , Three-phase equilibria , Critical endpoint , Triacontane , Hyperbaric reservoir fluids , Vapour–liquid equilibria
Journal title
Fluid Phase Equilibria
Serial Year
2004
Journal title
Fluid Phase Equilibria
Record number
1984665
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