Gas holdup and solid-liquid mass transfer in Newtonian and non-Newtonian fluids in bubble columns

被引：0
|
作者：
Ghosh, U. K. [1 ]
Upadhyay, S. N. [1 ]
机构：
[1] Banaras Hindu Univ, Inst Technol, Dept Chem Engn & Technol, Ctr Adv Study, Varanasi 221005, Uttar Pradesh, India
来源：
CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 2007年 / 85卷 / 06期
关键词：
bubble column; gas holdup; surface-liquid mast transfer; non-Newtonian fluids; wall-liquid heat and mass transfer coefficients;
D O I：
暂无
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
Gas holdup and surface-liquid mass transfer rate in a bubble column have been experimentally investigated. De-mineralized water, 0.5 and 1.0% aqueous solutions of carboxy methyl cellulose (CMC), and 60% aqueous propylene glycol have been used as the test liquids. Effects of column diameter, liquid height to column diameter ratio, superficial gas velocity and liquid phase viscosity on gas holdup and mass transfer rate are studied. Generalized correlations for the average gas holdup and wall to liquid heat and mass transfer coefficients are proposed. These are valid for both Newtonian and pseucloplastic non-Newtonian fluids.
引用
收藏
页码：825 / 832
页数：8
相关论文
共 50 条
12345