Vapor-Liquid Equilibriums of the Ternary System Chloroform-Methanol-Benzene

Jaime Wisniak; Abraham Tamir

doi:10.1021/je60079a014

Vapor-Liquid Equilibriums of the Ternary System Chloroform-Methanol-Benzene

Jaime Wisniak, Abraham Tamir

Department of Chemical Engineering

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3 Scopus citations

Abstract

New data of the vapor-liquid equllibria of the system chloroform-methanol-benzene were obtained at 760 mmHg. The activity coefficients were satisfactorily correlated according to the Redlich-Kister equation and could be predicted by considering only the binary data. Bolling points of the ternary mixture were predicted by an empirical correlation with a mean error of ±.12%. The system probably exhibits azeotropic behavior.

Original language	English
Pages (from-to)	287-292
Number of pages	6
Journal	Journal of Chemical & Engineering Data
Volume	23
Issue number	4
DOIs	https://doi.org/10.1021/je60079a014
State	Published - 1 Jan 1978

ASJC Scopus subject areas

Chemistry (all)
Chemical Engineering (all)

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title = "Vapor-Liquid Equilibriums of the Ternary System Chloroform-Methanol-Benzene",

abstract = "New data of the vapor-liquid equllibria of the system chloroform-methanol-benzene were obtained at 760 mmHg. The activity coefficients were satisfactorily correlated according to the Redlich-Kister equation and could be predicted by considering only the binary data. Bolling points of the ternary mixture were predicted by an empirical correlation with a mean error of ±.12%. The system probably exhibits azeotropic behavior.",

author = "Jaime Wisniak and Abraham Tamir",

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AU - Tamir, Abraham

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N2 - New data of the vapor-liquid equllibria of the system chloroform-methanol-benzene were obtained at 760 mmHg. The activity coefficients were satisfactorily correlated according to the Redlich-Kister equation and could be predicted by considering only the binary data. Bolling points of the ternary mixture were predicted by an empirical correlation with a mean error of ±.12%. The system probably exhibits azeotropic behavior.

AB - New data of the vapor-liquid equllibria of the system chloroform-methanol-benzene were obtained at 760 mmHg. The activity coefficients were satisfactorily correlated according to the Redlich-Kister equation and could be predicted by considering only the binary data. Bolling points of the ternary mixture were predicted by an empirical correlation with a mean error of ±.12%. The system probably exhibits azeotropic behavior.

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Vapor-Liquid Equilibriums of the Ternary System Chloroform-Methanol-Benzene

Abstract

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