Characteristics of Bubbly Flow, Mass Transfer, and CO2 Absorption in a Two-Stage Internal Loop Airlift Reactor Assembly with a Diamond-Shaped Guide Baffle

被引:3
|
作者
Song, Wenjie [1 ]
Zheng, Longyun [1 ]
Guo, Kai [1 ,5 ]
Liu, Hui [1 ,5 ]
Li, Wei [2 ]
Guo, Xiang [2 ]
Huang, Yiping [3 ]
Liu, Chunjiang [1 ,4 ,5 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
[2] Hubei Inst Aerosp Chemotechnol, Sci & Technol Aerosp Chem Power Lab, Xiangyang 441003, Hubei, Peoples R China
[3] China Construct Ind & Energy Engn Grp Co Ltd, Nanjing 210046, Jiangsu, Peoples R China
[4] Tianjin Univ, State Key Lab Chem Engn, Tianjin 300072, Peoples R China
[5] Tianjin Univ, Tianjin Key Lab Appl Catalysis Sci & Technol, Tianjin 300072, Peoples R China
基金
中国国家自然科学基金;
关键词
BACTERIAL CELLULOSE PRODUCTION; REGIME TRANSITIONS; GAS HOLDUP; ACETOBACTER-XYLINUM; IMMOBILIZED CELLS; SIZE DISTRIBUTION; HYDRODYNAMICS; REMOVAL; BEHAVIOR; IDENTIFICATION;
D O I
10.1021/acs.iecr.3c04139
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Airlift reactors are one of the most commonly used gas-liquid reactors in industry. The bubble flow regime, gas holdup, and bubble size are vital for mass transfer and chemical reaction in an airlift reactor. To improve the reactor performance, this study suggests a two-stage internal loop airlift reactor assembly with a diamond-shaped guide baffle. The hydrodynamic parameters, volumetric mass transfer coefficient, and the CO2 removal efficiency in the airlift reactor are measured. The effect of the guide baffle on the bubble flow regime, bubble size, gas holdup, mass transfer coefficient, and CO2 removal efficiency is investigated. Compared with a regular airlift reactor, the proposed airlift reactor features an increase in global gas holdup and volumetric mass transfer coefficients of up to 31.6 and 87.9%, respectively. Additionally, the CO2 removal efficiency increases in the airlift reactor assembly with the guide baffle.
引用
收藏
页码:4952 / 4964
页数:13
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