Implementation of PC-SAFT and SAFT plus Cubic for modeling thermodynamic properties of eight 1-alkenes and their mixtures

被引:17
|
作者
Polishuk, Ilya [1 ]
Perel, Ariel [1 ]
机构
[1] Ariel Univ Ctr Samaria, Dept Chem Engn & Biotechnol, IL-40700 Ariel, Israel
来源
JOURNAL OF CHEMICAL THERMODYNAMICS | 2012年 / 54卷
关键词
Olefins; Equation of state; Statistical association fluid theory; Density; Sound velocity; VAPOR-LIQUID-EQUILIBRIUM; COMPREHENSIVE DESCRIPTION; FISCHER-TROPSCH; STATE; HYDROCARBONS; PRESSURES; EQUATIONS; SYSTEMS; P; RHO; T; BINARY;
D O I
10.1016/j.jct.2012.03.023
中图分类号
O414.1 [热力学];
学科分类号
摘要
In the current study the widely used theoretically based model PC-SAFT and the recently proposed SAFT + Cubic have been implemented for correlating and predicting various thermodynamic properties of 1-Hexene, 1-Heptene, 1-Octene, 1-Nonene, 1-Decene, 1-Dodecene, 1-Tetradecene, and 1-Hexadecene, and the available high pressure data on their mixtures. Unlike PC-SAFT, SAFT + Cubic is capable of correlating the critical and subcritical pure compound data simultaneously. In addition, SAFT + Cubic is advantageous in predicting the isothermal compressibility factors and sound velocities. It is also superior in correlating the complex phase behavior in the asymmetric systems {Methane(1) + 1-Hexene(2)} and {Methane(1) + 1-Heptene(2)}. Overestimation of critical temperatures and pressures affects the accuracy of PC-SAFT in predicting VLE in the system {n-Hexane(1) + 1-Hexadecene(2)}. At the same time, this disadvantage of PC-SAFT possibly turns into advantage while modeling the VLE data of {Carbon Dioxide(1) + 1-Hexene(2)}. As seems, both of them are capable of only rough estimation of the heat capacity data. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:155 / 164
页数:10
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