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

Abraham Tamir; Jaime Wisniak

doi:10.1021/je60068a020

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

Abraham Tamir, Jaime Wisniak

Department of Chemical Engineering

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Abstract

Isobaric vapor-liquid equilibrium was measured for the system sec–butanol–isobutanol–n–butanol at 760 mm Hg with a Dvorak-Boublik recirculation apparatus. Liquid activity coefficients were evaluated for the three components and correlated with the Redlich-Kister and Wilson equations. 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)	91-94
Number of pages	4
Journal	Journal of Chemical & Engineering Data
Volume	21
Issue number	1
DOIs	https://doi.org/10.1021/je60068a020
State	Published - 1 Jan 1976

ASJC Scopus subject areas

Chemistry (all)
Chemical Engineering (all)

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

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

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

AB - Isobaric vapor-liquid equilibrium was measured for the system sec–butanol–isobutanol–n–butanol at 760 mm Hg with a Dvorak-Boublik recirculation apparatus. Liquid activity coefficients were evaluated for the three components and correlated with the Redlich-Kister and Wilson equations. 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 sec-Butanol–Isobutanol–n-Butanol

Abstract

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