The bubble size and rise velocity of bubble-induced three-phase inverse fluidized bed (BIFB)

被引:0
|
作者
Ma, Keying [1 ,2 ]
Sun, Zeneng [3 ]
Shao, Yuanyuan [4 ,5 ]
Zhu, Jesse [1 ,3 ,6 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin, Peoples R China
[2] Tianjin Univ, Zhejiang Inst, Shaoxing, Zhejiang, Peoples R China
[3] Univ Western Ontario, Dept Chem & Biochem Engn, London, ON, Canada
[4] Univ Nottingham Ningbo China, Nottingham Ningbo China Beacons Excellence Res & I, Ningbo, Zhejiang, Peoples R China
[5] Univ Nottingham Ningbo China, Nottingham Ningbo China Beacons Excellence Res & I, Ningbo 315100, Zhejiang, Peoples R China
[6] Univ Western Ontario, Dept Chem & Biochem Engn, London, ON N6A 3K7, Canada
关键词
bubble breakup; bubble coalescence; bubble rise velocity; bubble size; inverse fluidized bed; TURBULENT BED; HYDRODYNAMIC CHARACTERISTICS; WASTE-WATER; LIQUID; PHOTOGRAPHY; PERFORMANCE; PREDICTION; REACTOR;
D O I
10.1002/aic.18328
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The bubble size and rise velocity were investigated in detail using a new telecentric photographic probe in a pilot-scale bubble-induced three-phase inverse fluidized bed (BIFB). By the influence of the bubble flow behavior, the particle bed goes through four different flow regimes with increasing gas velocity in BIFB. An obvious normal bubble size distribution caused by bubble coalescence and breakup was observed. A parameter of "size span" was proposed to describe the distribution width of bubble size. The average bubble size increases with the axial distance from the column bottom and with the gas velocity until reaching a relatively stable size. The radial distributions of the average bubble size are almost uniform but experience a decreasing trend near the column wall. The bubble rise velocity increases with the bubble size and the gas velocity. An empirical equation was established to predict successfully the bubble rise velocity in BIFB.
引用
收藏
页数:10
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