Binary liquid-phase mass transport in mixed-bed ion exchange at low solute concentration

被引：13

作者：

Chowdiah, VN ^{[1
]}

Foutch, GL ^{[1
]}

Lee, GC ^{[1
]}

机构：

[1] Oklahoma State Univ, Sch Chem Engn, Stillwater, OK 74078 USA

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | 2003年 / 42卷 / 07期

关键词：

D O I：

10.1021/ie020668h

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

An accurate expression for ionic mass-transfer coefficients in ultrapure water is essential for detailed modeling and simulation of ion exchange. This paper presents an evaluation of 11 dimensionless mass-transfer correlations. Ten sets of experimental data, from both our laboratory and the literature, are used to define the best expression for ultrapure water applications. The correlation of Dwivedi and Upadhyay (Ind. Eng. Chem. Process Des. Dev. 1977, 16 (2), 157) gives the best results.

引用

页码：1485 / 1494

页数：10

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