Dynamic granular bed and its gas-solid separation process

被引:11
|
作者
Liu, Baigian [1 ,2 ]
Zhou, Wenning [1 ,2 ]
Tan, Peilai [1 ]
Shan, Xianghui [1 ]
Yang, Qianlong [1 ]
机构
[1] Univ Sci & Technol Beijing, Sch Mech Engn, Beijing 100083, Peoples R China
[2] Univ Sci & Technol Beijing, Beijing Key Lab Energy Saving & Emiss Reduct Met, Beijing 100083, Peoples R China
关键词
Granular bed filter; Gas filtration; Cake thickness; Collection efficiency; Flow patterns; Sublouvers; SYMMETRIC LOUVERED-WALL; FILTER BED; FLOW PATTERNS; FLUIDIZED-BED; FILTRATION; STRESSES; CLEANUP; TECHNOLOGY;
D O I
10.1016/j.powtec.2016.06.036
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, a new concept of dynamic granular bed was proposed based on the inertial number theory of powder mechanics. Compared with conventional moving granular bed, a fast-moving granular layer was formed on dynamic granular bed, which can capture the dust particulates and transport them away rapidly. The dust cake can be kept at a certain amount of thickness even after long-term operation. Hence the blowback process is not required in dynamic granular bed. Periodic working moving granular bed is then changed to continuous and steady working dynamic granular bed. Two kinds of dynamic granular beds were numerically and experimentally investigated in this work, i.e., vertical and inclined dynamic granular bed. It is found that inclined dynamic granular bed is superior to vertical dynamic granular bed. The experimental results show that there exist optimal parameters of both filtration superficial velocity and mass flow rate of filter granules for dynamic granular bed. Specifically the best collection efficiency occurred at a filtration superficial velocity of 0.3 m/s and a mass flow rate of 300 g/min for both vertical and inclined dynamic granular bed in the experiments. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:387 / 395
页数:9
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