Experimental investigation on bubble formation process in an aerated hopper

被引:2
|
作者
Zhong, Chongyi [1 ,2 ]
Guo, Xiaolei [1 ,2 ]
Xu, Jianliang [1 ,2 ]
Li, Weifeng [1 ,2 ]
Lu, Haifeng
Liu, Haifeng [1 ,2 ]
机构
[1] East China Univ Sci & Technol, Key Lab Coal Gasificat & Energy Chem Engn, Minist Educ, POB 272, Shanghai 200237, Peoples R China
[2] East China Univ Sci & Technol, Shanghai Engn Res Ctr Coal Gasificat, POB 272, Shanghai 200237, Peoples R China
基金
中国国家自然科学基金;
关键词
Aerated hopper; Bubble formation; Hopper discharge; FLUIDIZED-BED; PULVERIZED COAL; SINGLE ORIFICE; FINE POWDERS; DISCHARGE; FLOW; BEHAVIOR; MODEL; AIR; PARTICLES;
D O I
10.1016/j.powtec.2018.11.045
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The characteristics of the bubble formation in the process of powder discharge were investigated in a pseudo-2D aerated hopper by high-speed camera. The effects of particle size and gas velocity on the minimum bubble velocity, bubble growth, detachment and bubble formation frequency were systematically studied. Experimental results show that aeration can dramatically increase the discharge rate by up to about double, while the fluctuations of the powder discharge rate are also strengthened by bubbling as its standard deviation increases to more than 3 times that obtained without aeration. It appears that particle size and aeration gas velocity have significant effects in the aerated flowing hopper on the bubble formation process. With the increase of particle size, both the minimum bubble velocity and the formation frequency increase while the detach surface area, the maximum surface area and its lifespan decrease obviously, just like in a standard fluidized bed. Furthermore, comparison of the minimum bubble velocity with that in fluidized bed shows that it is easier to form bubble in aerated hopper and the velocity can be predicted by a revised model of the minimum fluidization velocity. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:237 / 244
页数:8
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