The Effect of Column Diameter and Bed Height on Minimum Fluidization Velocity

被引:66
作者
Rao, Akhil [1 ]
Curtis, Jennifer S. [1 ]
Hancock, Bruno C. [2 ]
Wassgren, Carl [3 ]
机构
[1] Univ Florida, Dept Chem Engn, Gainesville, FL 32611 USA
[2] Pfizer Global Res & Dev, Groton, CT 06340 USA
[3] Purdue Univ, Sch Mech Engn, W Lafayette, IN 47907 USA
关键词
minimum fluidization velocity; fluidized bed; column diameter; bed height; fluidization; PRESSURE-DROP; SEGREGATION; PARTICLES;
D O I
10.1002/aic.12161
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Experiments show that the minimum fluidization velocity of particles increases as the diameter of the fluidization column is reduced, or if the height of the bed is increased. These trends are shown to be due to the influence of the wall. A new, semi-correlated model is proposed, which incorporates Janssen's wall effects in the calculation of the minimum fluidization velocity. The wall friction opposes not only the bed weight but also the drag force acting on the particles during fluidization. The enhanced wall friction leads to an increase in the minimum fluidization velocity. The model predictions compare favorably to existing correlations and experimental data. (C) 2010 American Institute of Chemical Engineers AIChE J, 56: 2304-2311, 2010
引用
收藏
页码:2304 / 2311
页数:8
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