Hydrodynamics of a spouted bed with a porous draft tube containing a small amount of finer particles

被引:97
作者
Ishikura, T [1 ]
Nagashima, H [1 ]
Ide, M [1 ]
机构
[1] Fukuoka Univ, Fac Engn, Dept Chem Engn, Fukuoka 8140180, Japan
关键词
spouted beds; porous draft tube; binary particle mixtures; minimum spouting velocity; annulus gas flow rate; solids circulation rate;
D O I
10.1016/S0032-5910(02)00321-2
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A small-size spouted bed with a porous draft tube was employed to obtain hydrodynamic data of binary mixtures of glass beads for a range of operating conditions and design factors. In this case, a small amount of finer particles was added mostly to the large majority of coarser particles. Under this condition, minimum spouting velocity, bed pressure drop, hold-up of solid particles within a draft tube, gas flow rate through the annulus and solids circulation rate were determined by changing the total gas flow rate and the mass fraction of finer particles as operating parameters, and by changing the height of the entrainment zone and the draft tube diameter as geometric parameters. The results show that the gas flow rate through the annulus increases by increasing the distance between the gas inlet nozzle and the bottom of the draft tube, that is, the height of the entrainment zone, but decreases with increasing draft tube diameter and mass fraction of finer particles. The porous draft tube shows a higher gas flow rate through the annulus than the non-porous draft tube, particularly in the case of the low height of the entrainment zone. The solids circulation rate increases with increasing gas velocity, the height of the entrainment zone and the porous draft tube diameter. Moreover, the porous draft tube leads to a higher solids circulation rate than the non-porous draft tube. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:56 / 65
页数:10
相关论文
共 35 条
[1]   Minimum spouting velocity for binary mixture of particles in rectangular spouted beds [J].
Anabtawi, MZ .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1998, 76 (01) :132-136
[2]   SPOUTING WITH A POROUS DRAFT-TUBE [J].
CLAFLIN, JK ;
FANE, AG .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1983, 61 (03) :356-363
[3]  
CLAFLIN JK, 1984, AICHE S SER, V80, P17
[4]   FLUID-DYNAMICS CHARACTERIZATION OF A PNEUMATIC BED USING A SPOUTED BED TYPE SOLID FEEDING SYSTEM [J].
FERREIRA, MC ;
FREIRE, JT .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1992, 70 (05) :905-909
[5]  
Fukumori Y., 1997, J SOC POWDER TECHNOL, V34, P536
[6]  
Hadzismajlovic Dz, 1992, P 7 ENG FDN C FLUID, P337
[7]   Catalytic coal gasification using a draft tube spouted bed gasifier [J].
Hatate, Y ;
Mihara, H ;
Ijichi, K ;
Yoshimi, T ;
Arimizu, S ;
Uemura, Y ;
King, DF .
KAGAKU KOGAKU RONBUNSHU, 1996, 22 (05) :1180-1184
[8]  
HATATE Y, 1997, J SOC POWDER TECHNOL, V34, P343
[9]   Spouted bed with a draft tube without gas inlet nozzle or orifice [J].
Hattori, H ;
Nagai, T .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1996, 29 (03) :484-487
[10]  
HATTORI H, 1990, 55 M SOC CHEM ENG JA, P487