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首页> 外文期刊>Fluid Phase Equilibria >Liquid-vapour and solid-fluid equilibria for the system methane plus triacontane at high temperature and high pressure
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Liquid-vapour and solid-fluid equilibria for the system methane plus triacontane at high temperature and high pressure

机译:甲烷和金刚烷在高温高压下的液-气和固-液平衡

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摘要

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 (s(C30) + (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 x(C30) = 0.0275 +/- 0.002. (C) 2004 Elsevier B.V. All rights reserved.
机译:在这项工作中,给出了13种甲烷+金刚烷体系的不同组成的实验性汽-液和固-液平衡数据。该数据涵盖了从315到450 K的温度范围以及高达200 MPa的压力。研究的组成范围从几乎纯净的甲烷到纯净的三aco烷。根据主要的实验两相平衡结果,得出了三相曲线的过程(固体金刚烷+液体+蒸气)。在T = 340.73 +/- 0.4 K,P = 128.55 +/- 0.5处发现了该曲线的第二个关键终点,其中固体金刚烷与临界流体相处于平衡状态(s(C30)+(l = g)) MPa和临界流体相中的摩尔分数x(C30)= 0.0275 +/- 0.002。 (C)2004 Elsevier B.V.保留所有权利。

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