Effect of superficial gas velocity on solid behaviors in a full-loop CFB

被引:40
作者
Wang, Shuai [1 ]
Luo, Kun [1 ]
Hu, Chenshu [1 ]
Sun, Liyan [1 ]
Fan, Jianren [1 ]
机构
[1] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China
基金
中国国家自然科学基金; 国家重点研发计划;
关键词
Full-loop circulating fluidized bed; Solid mixing and dispersion; Solid residence time; Solid force and velocity; Particle granular temperature; CIRCULATING FLUIDIZED-BED; RESIDENCE TIME DISTRIBUTION; DISCRETE PARTICLE SIMULATION; RECTANGULAR SPOUTED BED; EULER-LAGRANGE APPROACH; SQUARE CROSS-SECTION; HIGH-DENSITY RISER; GRANULAR TEMPERATURE; NUMERICAL-SIMULATION; COUPLING APPROACH;
D O I
10.1016/j.powtec.2018.04.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effect of superficial gas velocity (Uf) on solid behaviors in a full-loop circulating fluidized bed is numerically studied using computational fluid dynamics-discrete element method (CFD-DEM). Specifically, the solid mixing and dispersion, solid residence time, solid force and velocity, and particle granular temperature are comprehensively explored. The results show that increasing Uf slows the solid mixing. The solid axial dispersion in the riser is dominated among that in the three regions. Besides, increasing Uf decreases the solid cycle time and leads to a more uniform solid residence time (SRT) distribution in the riser and dipleg. The fluid force is an order of magnitude smaller than the collision force. Increasing Uf shows distinctive influences on the rotational speed and translational velocity in the three regions. Moreover, increasing Uf suppresses the particle granular temperature. The average particle granular temperatures in the riser at four superficial gas velocities (i.e., 5.5 m/s, 6.0 m/s, 6.5 m/s, and 7.0 m/s) are 0.09326 m(2)/s(2), 0.08040 m(2)/s(2), 0.06531 m(2)/s(2), and 0.05047 m(2)/s(2), respectively. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:91 / 105
页数:15
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