Vapor-liquid equilibria and excess properties for methyl tert-butyl ether (MTBE) containing binary systems

被引:50
|
作者
Park, SJ [1 ]
Han, KJ
Gmehling, J
机构
[1] Chungnam Natl Univ, Coll Engn, Dept Chem Engn, Taejon 305764, South Korea
[2] Univ Oldenburg, D-26111 Oldenburg, Germany
关键词
methyl tert-butyl ether (MTBE); vapor-liquid equilibria; activity coefficient; excess molar property; infinite dilution; correlation;
D O I
10.1016/S0378-3812(02)00047-X
中图分类号
O414.1 [热力学];
学科分类号
摘要
Methyl tert-butyl ether (MTBE) is recently widely used in the chemical and petrochemical industry as a non-polluting octane booster for gasoline and as an organic solvent. The isobaric or isothermal vapor-liquid equilibria (VLE) were determined directly for MTBE + C-1-C-4 alcohols. The excess enthalpy (H-E) for butane + MTBE or isobutene + MTBE and excess volume (V-E) for MTBE + C-3-C-4 alcohols were also determined. Besides, the infinite dilute activity coefficient, partial molar excess enthalpies and volumes at infinite dilution (gamma(infinity), H-E,H-infinity, V-E.infinity) were calculated from measured data. Each experimental data were correlated with various g(E) models or empirical polynomial. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:399 / 409
页数:11
相关论文
共 50 条
  • [1] Isothermal vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons
    Lozano, LM
    Montero, EA
    Martin, MC
    Villamanan, MA
    FLUID PHASE EQUILIBRIA, 1997, 133 (1-2) : 155 - 162
  • [2] Vapor-liquid equilibria and vapor pressure data for the systems ethyl tert-butyl ether + ethanol and ethyl tert-butyl ether + water
    Rarey, Jürgen
    Horstmann, Sven
    Gmehling, Jürgen
    Journal of Chemical and Engineering Data, 44 (03): : 532 - 538
  • [3] VAPOR-LIQUID-EQUILIBRIA AND EXCESS VOLUMES FOR BINARY-SYSTEMS OF METHYL TERT-BUTYL ETHER (MTBE) WITH TRANS-1,2-DICHLOROETHYLENE AND ACETONITRILE
    MATO, FA
    BERRO, C
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1991, 36 (03): : 262 - 264
  • [4] Vapor-liquid equilibria at 101.32 kPa and excess properties of binary mixtures of butyl esters plus tert-butyl alcohol
    Ortega, J
    Espiau, F
    Postigo, M
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (02): : 444 - 454
  • [5] Vapor-liquid equilibria for the ternary systems of methyl tert-butyl ether plus methanol plus benzene and methyl tert-butyl ether plus methanol plus toluene and constituent binary systems at 313.15 K
    Oh, JH
    Han, KJ
    Won, DB
    Park, SJ
    FLUID PHASE EQUILIBRIA, 2003, 209 (02) : 215 - 228
  • [6] Vapor-liquid equilibria for methyl tert-butyl ether plus methanol and tert-amyl methyl ether plus methanol
    Toghiani, RK
    Toghiani, H
    Venkateswarlu, G
    FLUID PHASE EQUILIBRIA, 1996, 122 (1-2) : 157 - 168
  • [7] 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
  • [8] Measurement and correlation of isobaric vapor-liquid equilibria for binary and ternary systems containing Methyl Tertiary Butyl Ether (MTBE), methanol and alkanes
    Toru Watanabe
    Katsumi Honda
    Yasuhiko Arai
    Korean Journal of Chemical Engineering, 2003, 20 : 906 - 910
  • [9] Measurement and correlation of isobaric vapor-liquid equilibria for binary and ternary systems containing methyl tertiary butyl ether (MTBE), methanol and alkanes
    Watanabe, T
    Honda, K
    Arai, Y
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2003, 20 (05) : 906 - 910
  • [10] Isothermal vapor-liquid equilibria for mixtures of methyl tert-butyl ether, methyl acetate, and ethyl acetate
    Lee, MJ
    Hsiao, CC
    Lin, HM
    FLUID PHASE EQUILIBRIA, 1997, 137 (1-2) : 193 - 207