Volume 11 Issue 6
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Zhao, W., Wang, T., Wang, C., & Sha, Z. (2013). Hydrodynamic behavior of an internally circulating fluidized bed with tubular gas distributors. Particuology, 11(6), 664–672. https://doi.org/10.1016/j.partic.2012.05.012
Hydrodynamic behavior of an internally circulating fluidized bed with tubular gas distributors
Wenli Zhao a b, Tiefeng Wang a, Chenjing Wang a, Zuoliang Sha b *
a Beijing Key Laboratory of Green Reaction Engineering and Technology, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
b Tianjin Key Laboratory of Marine Resources and Chemistry, Tianjin University of Science and Technology, Tianjin 300457, China
10.1016/j.partic.2012.05.012
Volume 11, Issue 6, December 2013, Pages 664-672
Received 21 January 2012, Revised 21 April 2012, Accepted 11 May 2012, Available online 28 February 2013.
E-mail: zsha@tust.edu.cn

Highlights

► The internally circulating fluidized bed with a tubular distributor was studied. 

► While varying operating conditions, Gs and γDR follow a similar trend, but γDR is opposite to γDR. 

γDR was smaller than 10%, and may be decreased further. 

► Correlations were obtained to predict Gs, γDR and γDR.

Abstract

To better understand the hydrodynamic behavior of an internally circulating fluidized bed, solids holdup in the down-comer (ɛsD), solids circulation rate (Gs) and gas bypassing fraction (from down-comer to riser γDR, and from riser to down-comer γRD) were experimentally studied. The effects of gas velocities in the riser and in the down-comer (UR and UD), orifice diameter in the draft tube (dor), and draft tube height (HR) were investigated. Experimental results showed that increase of gas velocities led to increase in Gs and γDR, and slight decrease in γRD. Larger orifice diameter on the draft tube led to higher ɛsD, Gs and γDR, but had insignificant influence on γRD. With increasing draft tube height, both Gs and γDR first increased and then decreased, while γRD first decreased and then increased. Proposed correlations for predicting the hydrodynamic parameters agreed reasonably well with experimental values.

Graphical abstract
Keywords
Internally circulating fluidized bed; Solids holdup; Solids circulation rate; Gas bypassing fraction