Vapor-Liquid Equilibria of Isobutanol–n-Butanol and Isopropanol–sec-Butanol Systems

Abraham Tamir; Jaime Wisniak

doi:10.1021/je60067a010

Vapor-Liquid Equilibria of Isobutanol–n-Butanol and Isopropanol–sec-Butanol Systems

Abraham Tamir, Jaime Wisniak

Department of Chemical Engineering

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

10 Scopus citations

Abstract

Vapor-liquid equilibria data are measured at 760 mm Hg for the systems isobutanol-n-butanol and isopropanol-sec-butanol. Both systems exhibit slight positive deviations from ideal solution behavior, and their activity coefficients can be correlated by a two-constant Redlich-Kister equation. Boiling points of the mixtures are adequately described by a two-constant equation.

Original language	English
Pages (from-to)	391-392
Number of pages	2
Journal	Journal of Chemical and Engineering Data
Volume	20
Issue number	4
DOIs	https://doi.org/10.1021/je60067a010
State	Published - 1 Oct 1975

ASJC Scopus subject areas

General Chemistry
General Chemical Engineering

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title = "Vapor-Liquid Equilibria of Isobutanol–n-Butanol and Isopropanol–sec-Butanol Systems",

abstract = "Vapor-liquid equilibria data are measured at 760 mm Hg for the systems isobutanol-n-butanol and isopropanol-sec-butanol. Both systems exhibit slight positive deviations from ideal solution behavior, and their activity coefficients can be correlated by a two-constant Redlich-Kister equation. Boiling points of the mixtures are adequately described by a two-constant equation.",

author = "Abraham Tamir and Jaime Wisniak",

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AU - Tamir, Abraham

AU - Wisniak, Jaime

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Y1 - 1975/10/1

N2 - Vapor-liquid equilibria data are measured at 760 mm Hg for the systems isobutanol-n-butanol and isopropanol-sec-butanol. Both systems exhibit slight positive deviations from ideal solution behavior, and their activity coefficients can be correlated by a two-constant Redlich-Kister equation. Boiling points of the mixtures are adequately described by a two-constant equation.

AB - Vapor-liquid equilibria data are measured at 760 mm Hg for the systems isobutanol-n-butanol and isopropanol-sec-butanol. Both systems exhibit slight positive deviations from ideal solution behavior, and their activity coefficients can be correlated by a two-constant Redlich-Kister equation. Boiling points of the mixtures are adequately described by a two-constant equation.

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U2 - 10.1021/je60067a010

DO - 10.1021/je60067a010

M3 - Article

AN - SCOPUS:0345001231

SN - 0021-9568

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JO - Journal of Chemical and Engineering Data

JF - Journal of Chemical and Engineering Data

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ER -

Vapor-Liquid Equilibria of Isobutanol–n-Butanol and Isopropanol–sec-Butanol Systems

Abstract

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