Mass transfer in gas-liquid Couette-Taylor flow reactor

被引：31

作者：

Dluska, E ^{[1
]}

Wronski, S ^{[1
]}

Hubacz, R ^{[1
]}

机构：

[1] Warsaw Univ Technol, Fac Chem & Proc Engn, Ul Warynskiego 1, PL-00645 Warsaw, Poland

来源：

CHEMICAL ENGINEERING SCIENCE | 2001年 / 56卷 / 03期

关键词：

gas-liquid helicoidal flow; mass transfer;

D O I：

10.1016/S0009-2509(00)00331-6

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The results of the measurements of mass transfer coefficients for the physical (CO2/water) and chemical absorption (oxidation of benzaldehye) have been presented. The collected experimental data have been correlated with the energy dissipated in the system. High values of the mass transfer coefficients, k(L)a, of the order of 10(-1) s(-1) have been obtained. (C) 2001 Elsevier Science Ltd. All rights reserved.

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页码：1131 / 1136

页数：6

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