CHARACTERIZATION OF GAS-LIQUID PARAMETERS IN A DOWN-FLOW JET LOOP BUBBLE COLUMN

被引：32

作者：

Mandal, Ajay ^{[1
]}

机构：

[1] Indian Sch Mines, Dept Petr Engn, Dhanbad 826004, Bihar, India

来源：

BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING | 2010年 / 27卷 / 02期

关键词：

Bubble column; Down-flow; Bubble size; Interfacial area; Mass transfer coefficient; MASS-TRANSFER COEFFICIENT; INTERFACIAL AREA; HOLDUP DISTRIBUTION; ENTRAINMENT RATE; CHEMICAL METHODS; DISPERSED PHASE; SIZE; REACTORS; EJECTOR; HYDRODYNAMICS;

D O I：

10.1590/S0104-66322010000200004

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

In order to characterize the gas-liquid parameters of a down-flow jet loop reactor, experiments were carried out to study the gas holdup, bubble sizes and their distribution, mass transfer area and mass transfer coefficient. The experiments were performed in the bubbly flow regime because of its stability and uniformity. Analysis of experimental data showed an unambiguous relationship between gas holdup, bubble size, bubble size distribution and interfacial area. It has also been found that gas holdup and interfacial area is a strong function of slip velocity. The variation of interfacial area and mass transfer coefficient were also analyzed and expressed as a function of operational and geometric parameters.

引用

页码：253 / 264

页数：12

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