Statistical study of the distribution of voidage in a bubbling fluidized bed with a constant section

被引:4
作者
Yu, Shijie [1 ]
Yang, Xiaoxiao [1 ]
Xiang, Jie [1 ]
Li, Qinghai [1 ]
Zhou, Hui [1 ]
Zhang, Yanguo [1 ]
机构
[1] Tsinghua Univ, Key Lab Thermal Sci & Power Engn, Beijing Key Lab Utilizat & Reduct Technol CO2, Minist Educ,Dept Energy & Power Engn, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Voidage; Distribution; Statistics; Bubbling fluidized bed; Constant section; DYNAMIC-BEHAVIOR; FLOW REGIME; VELOCITY; DENSITY;
D O I
10.1016/j.cherd.2021.05.020
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The distribution of voidage was statistically studied in a plexiglass bubbling fluidized bed with a constant section. Four statistics, including average, standard deviation, skewness, and kurtosis, were analyzed. The vertical, horizontal, and three-dimensional distributions of voidage with various gas velocities were investigated. The results showed that both the vertical and horizontal distributions of voidage were more discrete for high gas velocities, i.e., the difference between different positions was greater. At the highest gas velocity, both voidage and the bubble size reached the maximum in the upper bed center. The minimum of voidage occurred near the upper bed wall, and the bubble was small both at the bottom and near the wall. The region of the sufficient bubbling fluidization was the maximum region of voidage, while the region of the particulate fluidization was the minimum region of voidage. (c) 2021 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:305 / 316
页数:12
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