Isothermal vapor-liquid equilibrium and excess enthalpy data for the binary systems diethyl ether + ethyl tert-butyl ether, 1-pentene + methyl acetate, and propene + 2-propanol

被引：0
|
作者：
Horstmann, Sven [1 ]
Gardeler, Hergen [1 ]
Bölts, Rainer [1 ]
Rarey, Jürgen [1 ]
Gmehling, Jürgen [1 ]
机构：
[1] Carl Von Ossietzky Universitaet O., Technische Chemie, Postfach 2503, D-26111 Oldenburg, Germany
来源：
Journal of Chemical and Engineering Data | / 44卷 / 03期
关键词：
D O I：
暂无
中图分类号：
学科分类号：
摘要：
引用
收藏
页码：383 / 387
相关论文
共 50 条
  • [41] Isobaric vapor-liquid equilibrium in the systems methyl 1,1-dimethylethyl ether+2-methyl-2-propanol and methyl 1,1-dimethylethyl ether+2-methylpentane+2-methyl-2-propanol
    Loras, S
    Aucejo, A
    Muñoz, R
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1999, 44 (06): : 1169 - 1174
  • [42] Thermodynamics of octane-enhancing additives in gasolines: Vapor-liquid equilibrium of the ternary mixtures methyl tert-butyl ether plus heptane plus benzene and methyl tert-butyl ether plus benzene plus 1-hexene at 313.15 K
    Segovia, JJ
    Martin, MC
    Chamorro, CR
    Villamanan, MA
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1998, 43 (06): : 1014 - 1020
  • [43] Vapor-liquid equilibrium of binary mixtures containing ethyl acetate plus 2-methyl-1-propanol and ethyl acetate plus 2-methyl-1-butanol at 101.3 kPa
    Resa, JM
    Goenaga, JM
    Lanz, J
    Iglesias, M
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2006, 51 (02): : 595 - 598
  • [44] Vapor-liquid equilibria for the binary system hexan-1-ol plus tert-butyl methyl ether (MTBE) at 298.15, 318.15, and 338.15 K
    de Llano, JJ
    Segade, L
    Jiménez, E
    del Río, A
    Renuncio, JAR
    Pando, C
    FLUID PHASE EQUILIBRIA, 2003, 208 (1-2) : 115 - 121
  • [45] Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of tert-Butanol plus tert-Butyl Acetate plus Chlorobenzene at 101.33 kPa
    Fan, Kai
    Zhou, Feng
    Chen, Changxu
    Li, Ye
    Li, Weisong
    Xiao, Bo
    Xu, Chunjian
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2018, 63 (08): : 2637 - 2643
  • [46] Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
    Bernatova, Svatoslava
    Pavlicek, Jan
    Wichterle, Ivan
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2011, 56 (04): : 783 - 788
  • [47] High pressure vapor-liquid equilibria of methyl acetate or ethyl acetate with 2-propanol at 1.5 MPa. Experimental data and predictions
    Susial, Rodrigo
    Susial, Pedro
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2015, 102 : 337 - 344
  • [48] Liquid-liquid equilibria for the ternary systems water plus 3-methyl-2-cyclopentenone with ethyl acetate or methyl tert-butyl ether at 293.2 K
    Choe, J
    Lee, H
    Kim, IW
    Hong, SH
    Song, KH
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (06): : 2028 - 2030
  • [49] Isothermal vapour-liquid equilibria in the binary and ternary systems composed of tert-butyl methyl ether, 3,3-dimethyl-2-butanone and 2,2-dimethyl-1-propanol
    Bernatova, Svatoslava
    Pavlicek, Jan
    Wichterle, Ivan
    FLUID PHASE EQUILIBRIA, 2009, 278 (1-2) : 129 - 134
  • [50] Isobaric vapor-liquid equilibrium in the systems methyl 1,1-dimethylethyl ether + 2-methyl-2-propanol and methyl 1,1-dimethylethyl ether + 2-methylpentane + 2-methyl-2-propanol
    Loras, Sonia
    Aucejo, Antonio
    Muñoz, Rosa
    Journal of Chemical and Engineering Data, 44 (06): : 1169 - 1174
12345