Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons .1. Total-pressure data and G(E) for methyl tert-butyl ether-benzene-cyclohexane at 313.15 K

被引：53

作者：

Segovia, JJ ^{[1
]}

Martin, MC ^{[1
]}

Chamorro, CR ^{[1
]}

Villamanan, MA ^{[1
]}

机构：

[1] UNIV VALLADOLID,ETS INGN IND,LAB TERMODINAM,DEPT INGN ENERGET & FLUIDOMECAN,E-47071 VALLADOLID,SPAIN

来源：

FLUID PHASE EQUILIBRIA | 1997年 / 133卷 / 1-2期

关键词：

VLE low pressure; hydrocarbons; MTBE; excess Gibbs energy;

D O I：

10.1016/S0378-3812(97)00011-3

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Isothermal P-x-y data for the ternary system (methyl tert-butyl ether (MTBE) + benzene + cyclohexane) and for its corresponding binaries at 40 degrees C are reported. Data reduction by Barker's method provides correlations for G(E), using the Margules equation for the binary systems and the Wohl expansion for the ternary system. (C) 1997 Elsevier Science B.V.

引用

页码：163 / 172

页数：10

共 4 条

[1] Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons 2.: Total-pressure data and GE for methyl tert-butyl ether/n-heptane/1-hexene at 313.15 K
Segovia, JJ
Martin, MC
Chamorro, CR
Montero, EA
Villamanan, MA
FLUID PHASE EQUILIBRIA, 1998, 152 (02) : 265 - 276
[2] Vapor-liquid equilibrium of ternary mixtures containing methyl tert-butyl ether and/or substitution hydrocarbons. Methyl tert-butyl ether plus heptane plus cyclohexane and methyl tert-butyl ether plus cyclohexane plus 1-hexene at 313.15 K
Segovia, JJ
Martin, MC
Chamorro, CR
Villamanan, MA
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1998, 43 (06): : 1021 - 1026
[3] Thermodynamic excess properties of the methyl tert-butyl ether plus benzene plus cyclohexane ternary system and its binary subsystems at temperature T = (293.15, 298.15, 303.15, and 313.15) K and ambient pressure
Llozana, Artan
Zeqiraj, Arber
Gjevori, Altin
Syla, Naim
Aliaj, Fisnik
PHYSICS AND CHEMISTRY OF LIQUIDS, 2024,
[4] Vapor-liquid equilibrium of octane-enhancing additives in gasolines 1.: Total pressure data and gE for binary and ternary mixtures containing di-isopropyl ether (DIPE), n-heptane and benzene at 313.15 K
Chamorro, CR
Segovia, JJ
Martín, MC
Villamañán, MA
FLUID PHASE EQUILIBRIA, 2001, 182 (1-2) : 229 - 239

← 1 →