详细信息

Effects of spherical adsorbent fluidization and self-rotation on removal of VOCs in a cyclonic fluidized bed  ( SCI-EXPANDED收录 EI收录)  

文献类型:期刊文献

英文题名:Effects of spherical adsorbent fluidization and self-rotation on removal of VOCs in a cyclonic fluidized bed

作者:Ma, Liang[1];Xiang, Guolin[1];Huang, Yuan[2];He, Mengya[1];Li, Jianping[1];Fu, Pengbo[1]

机构:[1]East China Univ Sci & Technol, Sch Mech & Power Engn, Shanghai 200237, Peoples R China;[2]East China Univ Sci & Technol, Sch Chem & Mol Engn, Shanghai 200237, Peoples R China

年份:2020

卷号:85

起止页码:181

外文期刊名:JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY

收录:;EI(收录号:20200908224028);WOS:【SCI-EXPANDED(收录号:WOS:000523605700016)】;

基金:We would like to express our thanks for the sponsorship of the National Key Research and Development Program of China (2016YFC0204500), National Natural Science Foundation of China (21878099, 51608203), Shanghai Sailing Program (19YF1412000) and the Fundamental Research Funds for the Central Universities (22221818014).

语种:英文

外文关键词:Cyclonic fluidized bed; VOC adsorption; Particle self-rotation; Activated carbon

摘要:A fluidized bed has the advantages of treating large flows, intensifying mass and heat transfer, and lowering costs. This study proposed a cyclonic fluidized bed packed with spherical activated carbon adsorbents for volatile organic compounds adsorption. The fluidization and self-rotation of the AC particles in a 25 mm cyclonic fluidized bed were studied with high-speed camera testing technology. The effects of the particle movement on the adsorption efficiency of toluene were also tested. The results show that most of the particles at the inlet side of the cyclonic fluidized bed were moving up when the inlet airflow rate was greater than 2.0 m 3 /h. The particles began to move in clusters when the relative packing height increased to a critical value of 0.57. Increasing the gas flow rate and the diameter and height of the core column will increase the self-rotation speed of the total particles. The maximum self-rotation speed of spherical adsorbents reached 1700 rad/s at the inlet flow rate of 2.5 m(3)/h. In the case of the same axial velocity of the gas phase in the upper space of the core column, increasing the particle self-rotation speed can slightly improve the adsorption efficiency. The maximum adsorption efficiency reached 99% when the inlet flow rate is 1.0 m(3)/h with relative packing height 0.65. (C) 2020 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.

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