Estimation of gas hold-up in aerated vessels

被引：23

作者：

Paglianti, A

Takenaka, K

Bujalski, W

Takahashi, K

机构：

[1] Univ Pisa, Dept Chem Engn, I-56126 Pisa, Italy

[2] Yamagata Univ, Dept Mat Sci & Engn, Yonezawa, Yamagata 992, Japan

[3] Univ Birmingham, Sch Chem Engn, Ctr Biochem Engn, Birmingham B15 2TT, W Midlands, England

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 2000年 / 78卷 / 02期

关键词：

gas hold-up; stirred vessel; single impeller; multiple-impeller; gas-liquid reactors;

D O I：

10.1002/cjce.5450780214

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

An attempt to produce a simple equation for gas hold-up in stirred tank reactors has been made. This new semi-empirical equation, based on the mass balance for the gas phase, predicts the observed effects due to the tank and impeller diameters and physical properties reasonably well. It can be used both for ranks working with a single Rushton impeller as well as with multiple Rushton impeller systems. The equation has been validated using both data found in literature and from our experiments.

引用

页码：386 / 392

页数：7

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