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摘要:
The external loop airlift reactor (EL-ALR) is widely used for gas-liquid reactions. It's advantage of good heat and mass transfer rates compared to conventional bubble column reactors. In the case of fermenta-tion application where a medium is highly viscous and coalescing in nature, internal in riser helps in the improvement of the interfacial area as well as in the reduction of liquid-phase back mixing. The compu-tational fluid dynamic (CFD) as a tool is used to design and scale-up of sectionalized external loop airlift reactor. The present work deals with computational fluid dynamics (CFD) techniques and experimental measurement of a gas hold-up, liquid circulation velocity, liquid axial velocity, Sauter mean bubble diam- eter over a broad range of superficial gas velocity 0.0024≤UG≤0.0168 m·s-1. The correlation has been made for bubble size distribution with specific power consumption for different plate configurations. The effects of an internal on different mass transfer models have been completed to assess their suitability. The predicted local mass transfer coefficient has been found higher in the sectionalized external loop air-lift reactor than the conventional EL-ALR.
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篇名 Experimental and Numerical Study of Gas-Liquid Flow in a Sectionalized External-Loop Airlift Reactor
来源期刊 中国化学工程学报(英文版) 学科
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年,卷(期) 2021,(4) 所属期刊栏目 Fluid Dynamics and Transport Phenomena
研究方向 页码范围 39-60
页数 22页 分类号
字数 语种 英文
DOI
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期刊影响力
中国化学工程学报(英文版)
月刊
1004-9541
11-3270/TQ
大16开
北京东城区青年湖南街13号
80-448
1982
eng
出版文献量(篇)
4237
总下载数(次)
1
总被引数(次)
21029
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