Prediction of isobaric vapour–liquid equilibrium from excess enthalpies for (methyl tert -butyl ether + alkane(s)) mixtures

2000 ◽  
Vol 32 (2) ◽  
pp. 175-186 ◽  
Author(s):  
Zhaohui Wang ◽  
Benjamin C.-Y. Lu
Keyword(s):  
Methyl Tert Butyl Ether ◽  
Excess Enthalpies ◽  
Liquid Equilibrium ◽  
Butyl Ether ◽  
Tert Butyl

Excess enthalpies of (ethanol or 1-propanol) + methyl tert-butyl ether + n -octane ternary mixtures at 298.15 K

1994 ◽  
Vol 94 ◽  
pp. 217-226 ◽  
Author(s):  
Shemin Zhu ◽  
Shubao Shen ◽  
George C. Benson ◽  
Benjamin C.-Y. Lu
Keyword(s):  
Ternary Mixtures ◽  
Methyl Tert Butyl Ether ◽  
Excess Enthalpies ◽  
Butyl Ether ◽  
Tert Butyl

Excess enthalpies of some (1-propanol + methyl tert-butyl ether + C6-hydrocarbon) ternary systems at 298.15 K

1994 ◽  
Vol 72 (4) ◽  
pp. 1111-1115 ◽  
Author(s):  
Shemin Zhu ◽  
Shubao Shen ◽  
George C. Benson ◽  
Benjamin C.-Y. Lu
Keyword(s):  
Ternary Systems ◽  
Methyl Tert Butyl Ether ◽  
Excess Enthalpies ◽  
Butyl Ether ◽  
Tert Butyl ◽  
Calorimetric Measurements

Calorimetric measurements of excess enthalpies are reported for the three ternary systems (1-propanol + methyl tert-butyl ether + (n-hexane, or 2,3-dimethylbutane, or cyclohexane)) at 298.15 K. Smoothing equations, fitted to the results, were used to construct constant enthalpy contours on a Roozeboom diagram for each of the systems.

Vapour-liquid equilibrium in the methyl tert-butyl ether-n-hexane and methyl tert-butyl ether-toluene systems

1979 ◽  
Vol 44 (12) ◽  
pp. 3627-3631 ◽  
Author(s):  
Jiří Plura ◽  
Jaroslav Matouš ◽  
Josef P. Novák ◽  
Josef Šobr
Keyword(s):  
Methyl Tert Butyl Ether ◽  
Liquid Equilibrium ◽  
Butyl Ether ◽  
Tert Butyl ◽  
Equilibrium Data ◽  
The One ◽  
Kister Equation

Vapour-liquid equilibrium data in binary methyl tert-butyl ether-n-hexane and methyl tert-butyl ether-toluene mixtures were determined experimentally. The data were described thermodynamically by the one-constant Redlich-Kister equation.

Excess enthalpies of ternary mixtures of an n-alkane with methyl tert-butyl ether and di-n-butyl ether

1997 ◽  
Vol 75 (3) ◽  
pp. 308-313 ◽  
Author(s):  
Zhangfa Tong ◽  
Dankui Liao ◽  
George C. Benson ◽  
Benjamin C. Y. Lu
Keyword(s):  
Ternary Systems ◽  
Excess Molar Enthalpies ◽  
Ternary Mixtures ◽  
Methyl Tert Butyl Ether ◽  
Excess Enthalpies ◽  
Butyl Ether ◽  
Flory Theory ◽  
Tert Butyl

Excess molar enthalpies, measured at 298.15 K, are reported for the two ternary systems consisting of either n-heptane or n-decane, together with methyl tert-butyl ether and di-n-butyl ether. Smooth representations of the results were used to construct constant enthalpy contours on Roozeboom diagrams. It was found that the Flory theory can provide good estimates of the ternary enthalpies. Keywords: excess enthalpies, ternary mixtures, n-alkanes, ethers, Flory theory.

Liquid-Liquid Equilibrium in the Water-Methyl tert-Butyl Ether-Nitromethane-Ethylene Glycol System

1993 ◽  
Vol 58 (5) ◽  
pp. 983-995
Author(s):  
Vladimír Kubíček ◽  
Josef P. Novák ◽  
Jaroslav Matouš
Keyword(s):  
Ethylene Glycol ◽  
Quaternary System ◽  
Calculated Data ◽  
Ternary Systems ◽  
Methyl Tert Butyl Ether ◽  
Liquid Equilibrium ◽  
Butyl Ether ◽  
Tert Butyl ◽  
Ternary Parameters

The liquid-liquid equilibrium was measured at 20 °C in the title quaternary system and in the three nitromethane-containing ternary subsystems. The data were compared with those predicted by a superposition of the Wilson and Redlich-Kister equations including the ternary parameters. The agreement between the observed and calculated data is very good both for the quaternary system and for the three ternary systems.

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