Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane plus sec-Butyl Acetate and Methylcyclohexane plus sec-Butyl Acetate under Atmosphere

被引:5
|
作者
Liu, Lixin [1 ]
Fu, Dianliang [2 ]
Sun, Yinhai [2 ]
Ma, Shoutao [2 ]
Sun, Lanyi [2 ]
机构
[1] Qingdao Univ Technol, Coll Mech Engn, Qingdao 266520, Shandong, Peoples R China
[2] China Univ Petr East China, Coll Chem Engn, State Key Lab Heavy Oil Proc, Qingdao 266580, Shandong, Peoples R China
来源
JOURNAL OF CHEMICAL AND ENGINEERING DATA | 2018年 / 63卷 / 05期
基金
中国国家自然科学基金;
关键词
101.3; KPA; EXPRESSION; MIXTURES; BENZENE; ENERGY;
D O I
10.1021/acs.jced.7b00999
中图分类号
O414.1 [热力学];
学科分类号
摘要
Data for two systems of isobaric vapor liquid equilibrium (VLE), n-heptane + sec-butyl acetate (SBAC) and methylcyclohexane + SBAC, were determined under atmosphere with an Ellis vapor liquid equilibrium still. The Herington method and Wisniak test were employed to determine the thermodynamic consistency of the two systems. The experimental results of n-heptane + SBAC and methylcyclohexane + SBAC were correlated by three activity coefficient models, which are the nonrandom two-liquid, universal quasichemical, and Wilson, and the correlation results fit well with experimental data. The binary interaction parameters of these models were obtained, and the results showed that these models can give good predictions. The VLE data provide theoretical basis and data support for the further study on separation of n-heptane + SBAC and methylcyclohexane + SBAC.
引用
收藏
页码:1403 / 1407
页数:5
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