Isobaric Vapor-Liquid Equilibria in the Ternary Systems Methyl Acetate + Vinyl Acetate + Propyl Bromide and Methyl Acetate + Vinyl Acetate + Toluene

Jaime Wisniak; Abraham Tamir

doi:10.1021/je00008a038

Isobaric Vapor-Liquid Equilibria in the Ternary Systems Methyl Acetate + Vinyl Acetate + Propyl Bromide and Methyl Acetate + Vinyl Acetate + Toluene

Jaime Wisniak, Abraham Tamir

Department of Chemical Engineering

Research output: Contribution to journal › Article › peer-review

Abstract

Vapor-liquid equilibrium at 101.3 kPa has been determined for the title systems. The data were correlated by the Redlich-Kister and Wisniak-Tamir equations, and the appropriate parameters are reported. The activity coefficients of the ternary systems can be predicted from those of the pertinent binary systems. No ternary azeotrope is present.

Original language	English
Pages (from-to)	538-541
Number of pages	4
Journal	Journal of Chemical and Engineering Data
Volume	37
Issue number	4
DOIs	https://doi.org/10.1021/je00008a038
State	Published - 1 Oct 1992

ASJC Scopus subject areas

General Chemistry
General Chemical Engineering

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10.1021/je00008a038

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title = "Isobaric Vapor-Liquid Equilibria in the Ternary Systems Methyl Acetate + Vinyl Acetate + Propyl Bromide and Methyl Acetate + Vinyl Acetate + Toluene",

abstract = "Vapor-liquid equilibrium at 101.3 kPa has been determined for the title systems. The data were correlated by the Redlich-Kister and Wisniak-Tamir equations, and the appropriate parameters are reported. The activity coefficients of the ternary systems can be predicted from those of the pertinent binary systems. No ternary azeotrope is present.",

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AU - Tamir, Abraham

PY - 1992/10/1

Y1 - 1992/10/1

N2 - Vapor-liquid equilibrium at 101.3 kPa has been determined for the title systems. The data were correlated by the Redlich-Kister and Wisniak-Tamir equations, and the appropriate parameters are reported. The activity coefficients of the ternary systems can be predicted from those of the pertinent binary systems. No ternary azeotrope is present.

AB - Vapor-liquid equilibrium at 101.3 kPa has been determined for the title systems. The data were correlated by the Redlich-Kister and Wisniak-Tamir equations, and the appropriate parameters are reported. The activity coefficients of the ternary systems can be predicted from those of the pertinent binary systems. No ternary azeotrope is present.

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U2 - 10.1021/je00008a038

DO - 10.1021/je00008a038

M3 - Article

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JO - Journal of Chemical and Engineering Data

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ER -

Isobaric Vapor-Liquid Equilibria in the Ternary Systems Methyl Acetate + Vinyl Acetate + Propyl Bromide and Methyl Acetate + Vinyl Acetate + Toluene

Abstract

ASJC Scopus subject areas

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