Radial gas mixing characteristics in a downer reactor

被引:9
作者
Bang, JH
Kim, YJ
Namkung, W
Kim, SD [1 ]
机构
[1] Korea Adv Inst Sci & Technol, Dept Chem Engn, Taejon 305701, South Korea
[2] Korea Adv Inst Sci & Technol, Energy & Environm Res Ctr, Taejon 305701, South Korea
关键词
fluidization; downer; circulating fluidized bed; radial das mixing; dispersion model;
D O I
10.1007/BF02708142
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In a downer reactor (0.1 m-I.D.x3.5 m-high), the effects of gas velocity (1.6-4.5 m/s), solids circulation rate (0-40 kg/m(2)s) and particle size (84, 164 mu m) on the gas mixing coefficient have been determined. The radial dispersion coefficient (D-r) decreases and the radial Peclet number (Pe(r)) increases as gas velocity increases. At lower gas velocities, D-r in the bed of particles is lower than that of gas flow only, but the reverse trend is observed at higher gas velocities. Gas mixing in the reactor of smaller particle size varies significantly with gas velocity, whereas gas mixing varies smoothly in the reactor of larger particle size. At lower gas velocities, D-r increases with increasing solids circulation rate (G(s)), however, D-r decreases with increasing G(s) at higher gas velocities. Based on the obtained D-r values, the downer reactor is found to be a good gas-solids contacting reactor having good radial gas mixing.
引用
收藏
页码:624 / 629
页数:6
相关论文
共 20 条
[1]   GAS MIXING IN GAS SOLIDS RISERS [J].
AMOS, G ;
RHODES, MJ ;
MINEO, H .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (05) :943-949
[2]  
AUBERT E, 1994, CIRCULATING FLUIDIZE, V4, P403
[3]  
Bader R., 1988, CIRCULATING FLUIDIZE, P123
[4]   THE AXIAL DISTRIBUTION OF THE CROSS-SECTIONALLY AVERAGED VOIDAGE IN FAST FLUIDIZED-BEDS [J].
BAI, DR ;
JIN, Y ;
YU, ZQ ;
ZHU, JX .
POWDER TECHNOLOGY, 1992, 71 (01) :51-58
[5]   Bed-to-wall heat transfer characteristics in a circulating fluidized bed [J].
Cho, YJ ;
Kim, SD ;
Han, GY .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 1996, 13 (06) :627-632
[6]   Radial gas mixing in a fast fluidized bed [J].
Gayan, P ;
deDiego, LF ;
Adanez, J .
POWDER TECHNOLOGY, 1997, 94 (02) :163-171
[7]  
Han G. Y., 1985, Korean Journal of Chemical Engineering, V2, P141
[8]  
Hirschfelder J.O., 1964, MOL THEORY GASES LIQ
[9]   DIFFUSION IN A FLUID MOVING AT UNIFORM VELOCITY IN A TUBE [J].
KLINKENBERG, A ;
KRAJENBRINK, HJ ;
LAUWERIER, HA .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (06) :1202-1208
[10]   GAS MIXING IN SLUGGING AND TURBULENT FLUIDIZED-BEDS [J].
LEE, GS ;
KIM, SD .
CHEMICAL ENGINEERING COMMUNICATIONS, 1989, 86 :91-111