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Hydrodynamic behavior of an internally circulating fluidized bed with tubular gas distributors 被引量:1
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作者 Wenli Zhao Tiefeng Wang +1 位作者 Chenjing Wang Zuoliang Sha 《Particuology》 SCIE EI CAS CSCD 2013年第6期664-672,共9页
To better understand the hydrodynamic behavior of an internally circulating fluidized bed, solids holdup in the down-comer (Eso), solids circulation rate (Gs) and gas bypassing fraction (from down-comer to riser ... To better understand the hydrodynamic behavior of an internally circulating fluidized bed, solids holdup in the down-comer (Eso), solids circulation rate (Gs) and gas bypassing fraction (from down-comer to riser y^R, and from riser to down-comer yRD) 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 yDR, and slight decrease in yeD. Larger orifice diameter on the draft tube led to higher 8sD, Gs and yDR, but had insignificant influence on YRD. with increasing draft tube height, both Gs and YDR first increased and then decreased, while yRD first decreased and then increased. Proposed correlations for predicting the hydrodynamic parameters agreed reasonably well with experimental values. 展开更多
关键词 Internally circulating fluidized bed Solids holdup Solids circulation rate gas bypassing fraction
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