High pressure phase behavior of methanol plus ethylene: Experimental measurements and CPA modeling

被引:4
作者
Karimi, Shahram [1 ]
Raeissi, Sona [1 ]
Florusse, Louw J. [2 ]
Peters, Cor J. [3 ,4 ]
机构
[1] Shiraz Univ, Sch Chem & Petr Engn, Shiraz 71345, Iran
[2] Delft Univ Technol, Fac Sci & Technol, Dept Chem Technol, NL-2628 BL Delft, Netherlands
[3] Petr Inst, Dept Chem Engn, Abu Dhabi, U Arab Emirates
[4] Eindhoven Univ Technol, Dept Chem & Chem Engn, Separat Technol Grp, NL-5612 AZ Eindhoven, Netherlands
关键词
Phase equilibria; Methyl alcohol; Ethene; Alkanol; Alkylene; Light olefin; Cubic-plus-association (CPA); Solvation; EQUATION-OF-STATE; LIQUID-LIQUID EQUILIBRIA; CARBON-DIOXIDE; FLUID MIXTURES; WATER; SYSTEMS; ETHENE; PROPANE; HYDROCARBONS; SEPARATION;
D O I
10.1016/j.supflu.2014.04.020
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
High pressure-temperature isopleths were obtained, experimentally, for the binary system of methanol + ethylene within a temperature and pressure range of 293-373 K and 38-119 bar, respectively. The experimental results were modeled using the Cubic-Plus-Association (CPA), Peng-Robinson (PR) and Soave-Redlich-Kwong (SRK) equations of state. The ability of the CPA model to predict the phase behavior of methanol + ethylene is much better than the SRK and PR models. However, even though the p-T diagrams indicate that the CPA equation of state correlates well with the experimental results, by increasing ethylene concentrations, the errors of CPA increase due to the solvation that occurs in methanol + ethylene systems. In this work, the effect of solvation is also investigated. Results show that deviations from experimental data are less for CPA with solvation than for the CPA without solvation. Correlations are presented for the binary interaction (k(ij)) and the association volume (beta(AiBj)) parameters to model the phase behavior of methanol + ethylene, as both of these parameters were indicated to be temperature-dependent. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:47 / 54
页数:8
相关论文
共 31 条
[1]   FLUID MIXTURES AT HIGH-PRESSURE - PHASE SEPARATION AND CRITICAL PHENOMENA IN BINARY-MIXTURES OF A POLAR COMPONENT WITH SUPERCRITICAL CARBON-DIOXIDE, ETHANE, AND ETHENE UP TO 1000 BAR [J].
ALWANI, Z ;
SCHNEIDER, GM .
BERICHTE DER BUNSEN-GESELLSCHAFT-PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1976, 80 (12) :1310-1315
[2]   SUPERCRITICAL FLUID EXTRACTION OF ALCOHOLS FROM WATER [J].
BRIGNOLE, EA ;
ANDERSEN, PM ;
FREDENSLUND, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (02) :254-261
[5]   Application of the CPA equation of state to organic acids [J].
Derawi, SO ;
Zeuthen, J ;
Michelsen, ML ;
Stenby, EH ;
Kontogeorgis, GM .
FLUID PHASE EQUILIBRIA, 2004, 225 (1-2) :107-113
[6]   Application of the CPA equation of state to glycol/hydrocarbons liquid-liquid equilibria [J].
Derawi, SO ;
Michelsen, ML ;
Kontogeorgis, GM ;
Stenby, EH .
FLUID PHASE EQUILIBRIA, 2003, 209 (02) :163-184
[7]   Extension of the cubic-plus-association equation of state to glycol-water cross-associating systems [J].
Derawi, SO ;
Kontogeorgis, GM ;
Michelsen, ML ;
Stenby, EH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (07) :1470-1477
[8]   Application of the cubic-plus-association (CPA) equation of state to complex mixtures with aromatic hydrocarbons [J].
Folas, GK ;
Kontogeorgis, GM ;
Michelsen, ML ;
Stenby, EH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (04) :1527-1538
[9]  
Ghanta M., 2008, THESIS KANSAS
[10]   High-pressure vapor-liquid equilibria for propane plus 2-butanol, propylene plus 2-butanol, and propane plus 2-butanol plus 2-propanol [J].
Gros, HP ;
Zabaloy, MS ;
Brignole, EA .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1996, 41 (02) :335-338