Isobaric Vapor-Liquid Equilibrium for Three Binary Systems of Acetaldehyde plus Ethanol, Ethyl Acetate, 1-Butanol at 101.3 kPa

被引：3
|
作者：
Sun, Huanhuan
Liu, Cheng
Geng, Zhongfeng [1 ]
Lu, Yang
Chen, Yixuan
机构：
[1] Tianjin Univ, Minist Educ, Res & Dev Ctr Petrochem Technol, Key Lab Green Chem Technol, Tianjin 300072, Peoples R China
来源：
JOURNAL OF CHEMICAL AND ENGINEERING DATA | 2017年 / 62卷 / 07期
关键词：
TERNARY MIXTURES; BUTADIENE; CONVERSION; CATALYSTS; 1,3-BUTADIENE; ACID; DEHYDROGENATION; BIOETHANOL; EXPRESSION; ALCOHOL;
D O I：
10.1021/acs.jced.7b00231
中图分类号：
O414.1 [热力学];
学科分类号：
摘要：
In this article, isobaric vapor liquid equilibrium (VLE) data for three binary systems of acetaldehyde + ethanol, acetaldehyde + ethyl acetate, and acetaldehyde +1-butanol were determined using a modified Rose Williams equilibrium still at 101.3 kPa. The experimental data were confirmed by the area method of Herington and point-to-point method of Van Ness. Activity coefficient models, Wilson, NRTL, and UNIQUAC were employed to correlate the experimental VLE values. Both models showed a good agreement and the binary interaction parameters were estimated.
引用
收藏
页码：2136 / 2142
页数：7
相关论文
共 50 条
  • [41] Isobaric vapor-liquid equilibria of binary system ethyl acetate plus ethyl benzene plus lithium bromide
    Al-Anber, Zaid Ahmed
    Kandah, Munther Issa
    Al-Shannag, Mohammad
    Al-Qodah, Zakaria
    Abu-Shaqra, Abdullah
    JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2013, 112 (02) : 953 - 959
  • [42] Isobaric Vapor-Liquid Equilibrium for the Extractive Distillation of Acetonitrile plus Water Mixtures Using Dimethyl Sulfoxide at 101.3 kPa
    Zhang, Zhigang
    Lv, Ming
    Huang, Donghao
    Jia, Peng
    Sun, Dezhang
    Li, Wenxiu
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2013, 58 (12): : 3364 - 3369
  • [43] Isobaric vapor-liquid equilibrium, density and speed of sound of binary mixtures 2,2,4-trimethylpentane+1-butanol or dibutyl ether (DBE) at 101.3 kPa
    Rubio-Perez, Gabriel
    Munoz-Rujas, Natalia
    Srhiyer, Adil
    Montero, Eduardo A.
    Aguilar, Fernando
    FLUID PHASE EQUILIBRIA, 2018, 475 : 10 - 17
  • [44] Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
    Gupta, Bhupender S.
    Lee, Ming-Jer
    FLUID PHASE EQUILIBRIA, 2012, 313 : 190 - 195
  • [45] Isobaric vapor-liquid equilibrium for binary systems of toluene plus o-xylene, benzene plus o-xylene, nonane plus benzene and nonane plus heptane at 101.3 kPa
    Gupta, Bhupender S.
    Lee, Ming-Jer
    FLUID PHASE EQUILIBRIA, 2013, 352 : 86 - 92
  • [46] Isobaric Vapor-Liquid Equilibrium for Binary Mixtures of 3-Methyl-1-butanol+3-Methyl-1-butyl Ethanoate and 1-Pentanol + Pentyl Ethanoate at 101.3 kPa
    Cepeda, Emilio A.
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55 (06): : 2349 - 2354
  • [47] Isobaric Vapor-Liquid Equilibria of Binary Systems (Propyl Acetate+2-Methylbutan-1-ol), (Propyl Acetate + Hexan-1-ol), and (Propyl Acetate + Heptan-1-ol) at 101.3 kPa
    Qi, Ye
    Liu, Yulong
    Xie, Jingwei
    Zhang, Minqing
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2014, 59 (08): : 2541 - 2546
  • [48] Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol plus n-Heptane and 1-Butanol + Aniline Binary Systems
    Alinejhad, Mehran
    Shariati, Alireza
    Hekayati, Javad
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2018, 63 (04): : 965 - 971
  • [49] Isobaric Vapor-Liquid Equilibrium for Binary System of Isoamyl DL-Lactate and Isoamyl Alcohol at 25.0, 50.0, and 101.3 kPa
    Xu, Jumei
    Li, Shating
    Zeng, Zuoxiang
    Xue, Weilan
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2020, 65 (01): : 81 - 87
  • [50] Isobaric Vapor-Liquid Equilibria for Binary Systems α-Phenylethylamine plus Toluene and α-Phenylethylamine plus Cyclohexane at 100 kPa
    Wu, Xiaoru
    Gao, Yingyu
    Ban, Chunlan
    Huang, Qiang
    RUSSIAN JOURNAL OF PHYSICAL CHEMISTRY A, 2016, 90 (09) : 1717 - 1723
12345