Isobaric low-pressure vapor-liquid equilibrium data of the system monochloroacetic acid plus dichloroacetic acid plus diethylene glycol dipentyl ether and the constituent binary systems

被引：4

作者：

Jongmans, Mark T. G. ^{[1
]}

Londono, Alex ^{[2
]}

Schuur, Boelo ^{[3
]}

de Haan, Andre B. ^{[1
]}

机构：

[1] Eindhoven Univ Technol, Proc Syst Engn Grp SPS, Chem Engn & Chem Dept, NL-5600 MB Eindhoven, Netherlands

[2] ISPT, NL-3800 AE Amersfoort, Netherlands

[3] Univ Twente, Fac Sci & Technol, Thermochem Convers Biomass Grp, NL-7500 AE Enschede, Netherlands

来源：

FLUID PHASE EQUILIBRIA | 2012年 / 334卷

关键词：

Vapor-liquid equilibrium; Acid-base interaction; Monochloroacetic acid; Dichloroacetic acid; Diethylene glycol dipentyl glyme; NRTL; Hayde-O'Connell; ACETIC-ACID; EXTRACTIVE DISTILLATION; SEPARATION; MIXTURES; BENZENE; PHASE; WATER;

D O I：

10.1016/j.fluid.2012.07.027

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

In this study, binary and ternary VLE data have been determined at 5, 7.5, and 10 kPa for the system monochloracetic acid (MCA) + dichloroacetic acid (DCA) + diethylene glycol dipentyl ether (DGDP). The extractant DGDP enhances the relative volatility of the MCA/DCA system from 1.2 without extractant up to 4. The non-ideal behavior in the liquid and vapor phase was reasonably well correlated with the NRTL and Hayden-O'Connell (HOC) model, respectively. The binary and ternary VLE data were correlated separately to obtain a better description of both datasets. (c) 2012 Elsevier B.V. All rights reserved.

引用

页码：15 / 21

页数：7

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