Vapor-liquid equilibrium of octane-enhancing additives in gasolines 1.: Total pressure data and gE for binary and ternary mixtures containing di-isopropyl ether (DIPE), n-heptane and benzene at 313.15 K

被引：14

作者：

Chamorro, CR ^{[1
]}

Segovia, JJ ^{[1
]}

Martín, MC ^{[1
]}

Villamañán, MA ^{[1
]}

机构：

[1] Univ Valladolid, ETS Ingenieros Ind, Dept Ingn Energet & Fluidomecan, Lab Termodinam & Calibrac, E-47071 Valladolid, Spain

来源：

FLUID PHASE EQUILIBRIA | 2001年 / 182卷 / 1-2期

关键词：

data; VLE low pressure; hydrocarbons; DIPE; excess Gibbs energy; correlations;

D O I：

10.1016/S0378-3812(01)00398-3

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Experimental isothermal P-x data at T = 313.15K for the ternary system (di-isopropyl ether (DIPE) + n-heptane + benzene) and for one of the previously unmeasured constituent binary systems, (DIPE + n-heptane), are reported. Data reduction by Barker's method provides correlations for g(E) using the Margules equation for the binary systems and the Wohl expansion for the ternary system. Wilson, NRTL and UNIQUAC models have been applied successfully to both the binary and the ternary systems. (C) 2001 Elsevier Science B.V. All rights reserved.

引用

页码：229 / 239

页数：11

共 27 条

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[2]

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