Particle size distribution in a granular bed filter

被引:8
|
作者
Du, Jianping [1 ]
Liu, Chuanping [1 ,2 ]
Yin, Shaowu [1 ,2 ]
Rehman, Ali [1 ]
Ding, Yulong [3 ,4 ]
Wang, Li [1 ,2 ]
机构
[1] Univ Sci & Technol Beijing, Sch Energy & Environm Engn, Beijing 100083, Peoples R China
[2] Univ Sci & Technol Beijing, Beijing Key Lab Energy Saving & Emiss, Reduct Met Ind, Beijing 100083, Peoples R China
[3] Univ Birmingham, Birmingham Ctr Energy Storage, Birmingham B15 2TT, W Midlands, England
[4] Univ Birmingham, Sch Chem Engn, Birmingham B15 2TT, W Midlands, England
来源
PARTICUOLOGY | 2021年 / 58卷
关键词
Granular bed; Multilayer filtration; Particle size distribution; Filtration superficial velocity; HOT GAS FILTRATION; POWER; ASH; EFFICIENCY; CLEANUP;
D O I
10.1016/j.partic.2021.01.016
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effects of the filtering granule particle size and filtration superficial velocity on the dust particle size distribution in different layers of a granular bed system are discussed herein. A multilayer drawer granular bed filtration system was designed for these experiments based on filtering fly ash from a power plant. After a 1-h experiment, 47.8% of dust particles smaller than 2.5 mu m, 63.7% of dust particles smaller than 10 mu m, and 39.1% of dust particles larger than 10 mu m were captured by the granular bed (corresponding to initial volume fractions of 6%, 19.3%, and 80.7%, respectively). Large dust particles were more easily trapped by the granular bed than small dust particles. Increasing the size of the filter granules and increasing the superficial velocity of the inlet flue gas were both effective ways to enhance the dust-holding capacity of the granular media throughout the granular bed. (c) 2021 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:108 / 117
页数:10
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