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

Author:

Ma Keying12,Sun Zeneng3ORCID,Shao Yuanyuan4,Zhu Jesse13ORCID

Affiliation:

1. School of Chemical Engineering and Technology Tianjin University Tianjin China

2. Zhejiang Institute of Tianjin University Shaoxing Zhejiang China

3. Department of Chemical & Biochemical Engineering The University of Western Ontario London Ontario Canada

4. Nottingham Ningbo China Beacons of Excellence Research and Innovation Institute The University of Nottingham Ningbo China Ningbo Zhejiang China

Abstract

AbstractThe 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.

Publisher

Wiley

Subject

General Chemical Engineering,Environmental Engineering,Biotechnology

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