Investigation of hydrodynamic performance in a staggered multistage internal airlift loop reactor

被引:7
|
作者
Wang, Weiwen [1 ]
Pan, Qingpeng [1 ]
Shen, Zongwang [1 ]
Dong, Yangshuo [2 ]
Zhou, Litong [1 ]
Yu, Zhixin [1 ]
Chen, Guanghui [1 ]
Duan, Jihai [1 ]
机构
[1] Qingdao Univ Sci & Technol, Coll Chem Engn, Key Lab Multiphase Fluid React & Separat Engn Sha, Qingdao 266042, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Environm & Safety Engn, Qingdao 266042, Peoples R China
关键词
MASS-TRANSFER CHARACTERISTICS; IMAGE MEASUREMENT TECHNIQUE; BUBBLE-SIZE DISTRIBUTIONS; CFD SIMULATION; MIXING CHARACTERISTICS; FLUID-DYNAMICS; WASTE-WATER; COLUMN; FLOW; BIOREACTOR;
D O I
10.1063/5.0190749
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
The multistage internal airlift loop reactor (MIALR) has shown promising application prospects in gas-liquid-solid reaction systems. However, traditional MIALRs have a global circulation with strong interstage liquid-phase exchange. This paper proposes a staggered multistage internal airlift loop reactor (SMIALR) that incorporates special guide elements to create a staggered flow. Both experiments and computational fluid dynamics-population balance model simulations were conducted to investigate the hydrodynamic performances of MIALR and SMIALR. The results demonstrate that SMIALR exhibits a local circulation at each stage. Bubbles have a longer residence time in SMIALR, resulting in a 28.35%-55.54% increase in gas holdup and a 7.27%-13.69% increase in volumetric mass transfer coefficient. The gas-liquid mass transfer coefficient of SMIALR was improved by increasing the gas-liquid interfacial area. Additionally, the radial distribution of solids was found to be more uniform. This study offers insights for optimizing MIALR and provides a theoretical foundation for the design and scale-up of SMIALR.
引用
收藏
页数:21
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