Vapor-liquid equilibria and excess volumes of the binary systems ethanol plus ethyl lactate, isopropanol plus isopropyl lactate and n-butanol plus n-butyl lactate at 101.325 kPa

被引:41
|
作者
Peña-Tejedor, S [1 ]
Murga, R [1 ]
Sanz, MT [1 ]
Beltrán, S [1 ]
机构
[1] Univ Burgos, Dept Ingn Quim, Burgos 09001, Spain
关键词
experimental data; vapor-liquid equilibrium; alcohols; lactates; excess volumes;
D O I
10.1016/j.fluid.2005.02.015
中图分类号
O414.1 [热力学];
学科分类号
摘要
Isobaric vapor-liquid equilibrium data have been experimentally determined at 101.3 kPa for the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate. No azeotrope was found in any of the systems. All the experimental data reported were thermodynamically consistent according to the point-to-point method of Fredenslund. The activity coefficients were correlated with the NRTL and UNIQUAC liquid-phase equations and the corresponding binary interaction parameters are reported. The densities and derived excess volumes for the three mixtures are also reported at 298.15 K. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:197 / 203
页数:7
相关论文
共 50 条
  • [31] Isobaric Vapor-Liquid Equilibrium for Three Binary Systems of Acetaldehyde plus Ethanol, Ethyl Acetate, 1-Butanol at 101.3 kPa
    Sun, Huanhuan
    Liu, Cheng
    Geng, Zhongfeng
    Lu, Yang
    Chen, Yixuan
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2017, 62 (07): : 2136 - 2142
  • [32] Study of Vapor-Liquid Equilibria for Acetic Acid plus n-Propyl Acetate plus Isopropyl Acetate Systems
    Li, Geng
    Yin, Xianqing
    Jing, Bo
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2019, 64 (06): : 2759 - 2766
  • [33] Isobaric vapor liquid equilibrium (VLE) data of the systems n-butanol plus butyric acid and n-butanol plus acetic acid
    Muñoz, LAL
    Krähenbühl, MA
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2001, 46 (01): : 120 - 124
  • [34] Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate plus Methanol, plus Ethanol, plus Dimethyl Carbonate, or plus Diethyl Carbonate at 101.3 kPa
    Zhang, Xuemei
    Zuo, Jian
    Jian, Chungui
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55 (11): : 4896 - 4902
  • [35] Correlation and Prediction for Isobaric Vapor-Liquid Equilibria of the Diethyl Ether plus Methanol+1-Butanol Ternary System and the Constituent Binary Systems at 101.325 kPa
    Gao, Daming
    Zhang, Hui
    Zhu, Dechun
    Sun, Hong
    Chen, Hong
    Shi, Jianjun
    Luecking, Peter
    Winter, Bernhard
    Zhan, Yamei
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (01) : 567 - 575
  • [36] Vapor-liquid equilibria for the ternary system benzene plus n-heptane plus N,N-dimethylformamide at 101.33 kPa
    Blanco, B
    Sanz, MT
    Beltrán, S
    Cabezas, JL
    Coca, J
    FLUID PHASE EQUILIBRIA, 2000, 175 (1-2) : 117 - 124
  • [37] Isobaric Vapor-Liquid Equilibria for Ethyl Acetate plus Methanol plus Ionic Liquids Ternary Systems at 101.3 kPa
    Zhang, Zhigang
    Pan, Fenjin
    Zhang, Qinqin
    Zhang, Tao
    Zhang, Lin
    Wu, Kaifang
    Li, Wenxiu
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2016, 61 (02): : 772 - 779
  • [38] Separation Effects of Renewable Solvent Ethyl Lactate on the Vapor-Liquid Equilibria of the Methanol plus Dimethyl Carbonate Azeotropic System
    Matsuda, Hiroyuki
    Inaba, Koji
    Nishihara, Keiji
    Sumida, Hirofumi
    Kurihara, Kiyofumi
    Tochigi, Katsumi
    Ochi, Kenji
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2017, 62 (09): : 2944 - 2952
  • [39] Isobaric vapor-liquid equilibrium data for the binary system methyl acetate plus isopropyl acetate and the quaternary system methyl acetate plus methanol plus isopropanol plus isopropyl acetate at 101.3 kPa
    Xiao, Li
    Wang, Qing-lian
    Wang, Hong-xing
    Qiu, Ting
    FLUID PHASE EQUILIBRIA, 2013, 344 : 79 - 83
  • [40] Vapor-liquid equilibria for water plus acetic acid plus (N,N-dimethylformamide or dimethyl sulfoxide) at 13.33 kPa
    Peng, Yong
    Ping, Lijuan
    Lu, Shengli
    Mao, Jianwei
    FLUID PHASE EQUILIBRIA, 2009, 275 (01) : 27 - 32