Phase equilibria in the systems oxolane plus octane and methyl 1,1-dimethylethyl ether plus hex-1-ene

被引：5

作者：

Wisniak, J ^{[1
]}

Fishman, E ^{[1
]}

Shaulitch, R ^{[1
]}

机构：

[1] Ben Gurion Univ Negev, Dept Chem Engn, IL-84105 Beer Sheva, Israel

来源：

JOURNAL OF CHEMICAL AND ENGINEERING DATA | 1998年 / 43卷 / 03期

关键词：

D O I：

10.1021/je970284b

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Vapor-liquid equilibrium at 94 kPa has been determined for the binary system oxolane + octane and methyl 1,1-dimethylethyl ether + hex-1-ene. The system oxolane + octane deviates strongly from ideality with no azeotrope formation. The system methyl 1,1-dimethylethyl ether + hex-1-ene presents ideal behavior. The activity coefficients of the system oxolane + octane were correlated reasonable well with its composition by the Redlich-Kister, Wohl, Wilson, UNIQUAC, and NRTL models. The boiling point of both binary systems were correlated with the Wisniak-Tamir equation.

引用

页码：304 / 306

页数：3

共 50 条

[1] Phase equilibria in the systems oxolane plus octane and methyl 1,1-dimethylethyl ether plus hex-1-ene. (vol 43, pg 304, 1998)
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JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1998, 43 (06): : 1107 - 1107
[2] Phase equilibria in the systems oxolane plus vinyl acetate, oxolane plus ethyl 1,1-dimethylethyl ether and vinyl acetate plus ethyl 1,1-dimethylethyl ether
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[4] Phase equilibria in the ternary system methyl 1,1-dimethylethyl ether plus hexane plus octane
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JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1998, 43 (03): : 307 - 311
[5] Phase equilibria in the ternary system methyl 1,1-dimethylethyl ether plus heptane plus octane
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[8] Isobaric vapor-liquid equilibria in the systems methyl 1,1-dimethylethyl ether plus octane and heptane plus octane
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[9] Isobaric vapor-liquid equilibria in the systems methyl 1,1-dimethylethyl ether plus methyl ethanoate and oxolane plus heptane
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[10] Phase equilibria in the ternary system ethyl 1,1-dimethylethyl ether plus heptane plus octane
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FLUID PHASE EQUILIBRIA, 1999, 154 (02) : 213 - 222

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