Phase equilibria of (CO2 + butylbenzene) and (CO2 + butylcyclohexane) at temperatures between (323.15 and 423.15) K and at pressures up to 21 MPa

被引:1
|
作者
Hou, Shu-Xin [1 ]
Maitland, Geoffrey C. [1 ]
Trusler, J. P. Martin [1 ]
机构
[1] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn, Qatar Carbonates & Carbon Storage Res Ctr, London SW7 2AZ, England
关键词
Phase equilibria; CO2; Butylbenzene; Butylcyclohexane; Peng-Robinson equation of state; Wong-Sandler mixing rules; CARBON-DIOXIDE; BEHAVIOR;
D O I
10.1016/j.fluid.2014.12.022
中图分类号
O414.1 [热力学];
学科分类号
摘要
Experimental measurements of the phase equilibria of (CO2 + butylbenzene) and (CO2 + butylcyclohexane) have been made with an analytical apparatus at temperatures of (323.15, 373.15 and 423.15) K at pressures from 2 MPa to the mixture critical pressure. These are the first results to be published for (CO2 + butylcyclohexane), while for (CO2 + butylbenzene) they are the first at pressures above 6 MPa. To model the data, we use the Peng-Robinson equation of state with Wong-Sandler mixing rules incorporating the NRTL equation. The model describes the measured bubble point curves very well at all temperatures, except close to the mixture critical points at high pressures. The dew point curves are described well only at the lowest temperature: otherwise, deviations increase in the approach to the mixture critical point. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:111 / 116
页数:6
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