Effect of Solid Particles on the Slurry Bubble Columns Behavior - A Review

被引:13
|
作者
Mahmoudi, Sadra [1 ]
Hlawitschka, Mark W. [1 ]
机构
[1] Johannes Kepler Univ Linz, Inst Proc Engn, Altenbergerstr 69, A-4040 Linz, Austria
来源
CHEMBIOENG REVIEWS | 2022年 / 9卷 / 01期
关键词
Flow regime; Gas hold-up; Mass transfer; Slurry bubble column; Solid particles; LIQUID MASS-TRANSFER; TRANSFER COEFFICIENT; GAS HOLDUP; TRANSFER ENHANCEMENT; ORGANIC LIQUIDS; RISE VELOCITIES; OXYGEN-TRANSFER; FLUIDIZED-BED; HEAT-TRANSFER; FLOW REGIME;
D O I
10.1002/cben.202100032
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A wide-ranging review is presented on the most focal aspects of gas-liquid-solid reactors to discuss the fresh headways towards the understanding of slurry bubble column reactors' behavior. In more detail, in this critical review, published works' findings concerning the effects of solid particles characteristics (size, concentration and density) on volumetric mass transfer coefficient, liquid-side mass transfer coefficient, gas-liquid interfacial area, gas hold-up and flow regime are deliberated. Besides, the effects of other pivotal parameters such as pressure, temperature, reactor size, height of liquid, gas distr1111111ibutor, density, and viscosity on the performance of slurry bubble column reactors are considered. Eventually, regarding the effects of each of the aforementioned parameters on the performance of reactor, logical conclusions are drawn.
引用
收藏
页码:63 / 92
页数:30
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