Ternary Vapor-Liquid Equilibria for System n-Butanol–sec-Butanol–tert-Butanol

Jaime Wisniak; Abraham Tamir

doi:10.1021/je60067a011

Ternary Vapor-Liquid Equilibria for System n-Butanol–sec-Butanol–tert-Butanol

Jaime Wisniak, Abraham Tamir

Department of Chemical Engineering

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1 Scopus citations

Abstract

Isobarlc vapor-liquid equilibrium was measured for the system n-butanol–sec-butanol–tert-butanol at 760 mm Hg with a Dvorak-Boublik recirculation still. Liquid activity coefficients were evaluated for the three components and correlated with a Redlich-Kister type equation. Vapor composition and boiling points were correlated from binary and ternary data and showed good agreement with the experimental information.

Original language	English
Pages (from-to)	393-396
Number of pages	4
Journal	Journal of Chemical and Engineering Data
Volume	20
Issue number	4
DOIs	https://doi.org/10.1021/je60067a011
State	Published - 1 Oct 1975

ASJC Scopus subject areas

General Chemistry
General Chemical Engineering

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title = "Ternary Vapor-Liquid Equilibria for System n-Butanol–sec-Butanol–tert-Butanol",

abstract = "Isobarlc vapor-liquid equilibrium was measured for the system n-butanol–sec-butanol–tert-butanol at 760 mm Hg with a Dvorak-Boublik recirculation still. Liquid activity coefficients were evaluated for the three components and correlated with a Redlich-Kister type equation. Vapor composition and boiling points were correlated from binary and ternary data and showed good agreement with the experimental information.",

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AU - Tamir, Abraham

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N2 - Isobarlc vapor-liquid equilibrium was measured for the system n-butanol–sec-butanol–tert-butanol at 760 mm Hg with a Dvorak-Boublik recirculation still. Liquid activity coefficients were evaluated for the three components and correlated with a Redlich-Kister type equation. Vapor composition and boiling points were correlated from binary and ternary data and showed good agreement with the experimental information.

AB - Isobarlc vapor-liquid equilibrium was measured for the system n-butanol–sec-butanol–tert-butanol at 760 mm Hg with a Dvorak-Boublik recirculation still. Liquid activity coefficients were evaluated for the three components and correlated with a Redlich-Kister type equation. Vapor composition and boiling points were correlated from binary and ternary data and showed good agreement with the experimental information.

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Ternary Vapor-Liquid Equilibria for System n-Butanol–sec-Butanol–tert-Butanol

Abstract

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