Flow structure and thickness of annular downflow layer in a circulating fluidized bed riser

被引:52
作者
Kim, SW [1 ]
Kirbas, G [1 ]
Bi, HT [1 ]
Lim, CJ [1 ]
Grace, JR [1 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, Vancouver, BC V6T 1Z4, Canada
关键词
circulating fluidized bed; fast fluidization; hydrodynamics; core-annulus structure; annular downflow layer thickness; momentum probe;
D O I
10.1016/j.powtec.2004.03.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Flow structures were determined in a circulating fluidized bed (CFB) riser (0.203 m i.d. x 5.9 m high) of FCC particles (d(p)=70 mum, rho(s)= 1700 kg/m(3)). A momentum probe was used to measure radial momentum flux profiles at several levels and to distinguish between upward and downward flow regions. Time-mean dynamic pressure (DeltaP(m)) decreases towards the wall in the range U-g=5-8 m/s, G(s)=10-340 kg/m(2) s. The thickness of the annular downflow layer based on DeltaP(m)=0 reaches a maximum with increasing height. The annular downflow layer disappears locally with increasing solids mass flux (G(s)) at a constant gas velocity, with achievement of the dense suspension upflow (DSU) regime. A new correlation is developed to predict the time-mean thickness of solids down-flowing layer based on solids mass flux and momentum flux. It successfully accounts for the variation of the annular layer thickness with height and Gs, and covers a wide Gs range right up to near the onset of the DSU regime. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:48 / 58
页数:11
相关论文
共 39 条
[1]  
Bader R., 1988, CIRCULATING FLUIDIZE, P123
[2]   DISTINCTION BETWEEN UPWARD AND DOWNWARD FLOWS IN CIRCULATING FLUIDIZED-BEDS [J].
BAI, D ;
SHIBUYA, E ;
MASUDA, Y ;
NISHIO, K ;
NAKAGAWA, N ;
KATO, K .
POWDER TECHNOLOGY, 1995, 84 (01) :75-81
[3]   Annular wall layer thickness in circulating fluidized bed risers [J].
Bi, HT ;
Zhou, J ;
Qin, SZ ;
Grace, JR .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1996, 74 (05) :811-814
[4]   FLOW REGIME DIAGRAMS FOR GAS-SOLID FLUIDIZATION AND UPWARD TRANSPORT [J].
BI, HT ;
GRACE, JR .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1995, 21 (06) :1229-1236
[5]  
COUTURIER M, 1991, 11 INT C FLUID BED C, P107
[6]  
GAJDOS LJ, 1978, FC24408 CARNEGIE MEL
[7]   Situating the high-density circulating fluidized bed [J].
Grace, JR ;
Issangya, AS ;
Bai, DR ;
Bi, HT ;
Zhu, JX .
AICHE JOURNAL, 1999, 45 (10) :2108-2116
[8]   Reflections on turbulent fluidization and dense suspension upflow [J].
Grace, JR .
POWDER TECHNOLOGY, 2000, 113 (03) :242-248
[9]  
GRACE JR, 1997, CIRCULATING FLUIDIZE, P504
[10]   Characterisation of the annular film thickness in circulating fluidised-bed risers [J].
Harris, AT ;
Thorpe, RB ;
Davidson, JF .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (13) :2579-2587