Vapor-liquid equilibrium for the carbon dioxide plus hydrogen plus methanol ternary system

被引：18

作者：

Bezanehtak, K ^{[1
]}

Dehghani, F ^{[1
]}

Foster, NR ^{[1
]}

机构：

[1] Univ New S Wales, Sch Chem Engn & Ind Chem, Sydney, NSW 2052, Australia

来源：

JOURNAL OF CHEMICAL AND ENGINEERING DATA | 2004年 / 49卷 / 03期

关键词：

D O I：

10.1021/je0301491

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Vapor-liquid equilibrium data for the ternary system carbon dioxide (CO2) + hydrogen (H-2) + methanol (MeOH) were determined at temperatures between 278 K and 298 K and pressures between 20 bar and 200 bar. A dynamic technique with vapor and liquid recirculation and on-line gas chromatography was used in this study.

引用

页码：430 / 434

页数：5

共 4 条

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INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (12) :4571-4579

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