Effects of various parameters on the attrition of bed material in a recirculating fluidized bed with a draft tube

被引:9
作者
Chourasia, Shivali [1 ]
Alappat, Babu J. [1 ]
机构
[1] Indian Inst Technol Delhi, Dept Civil Engn, New Delhi 110016, India
来源
PARTICUOLOGY | 2018年 / 38卷
关键词
Attrition; Recirculating fluidized bed (RCFB); Fluidization; Elutriation; Fines; SOLID CIRCULATION RATE; COAL ASH PARTICLES; SIZE DISTRIBUTION; CATALYST; REACTOR; MODEL; SYSTEMS;
D O I
10.1016/j.partic.2017.05.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We performed an experimental study to investigate the effects of various parameters on the attrition of bed material and its size distribution with increasing operation time in a recirculating fluidized bed (RCFB). The studied parameters included superficial velocity of fluidizing air, bed inventory, and spacing between the jet top and draft tube bottom (spacer height). The bed material was prepared from Indian Standard (IS) Grade I sand from sieves with a size range of 2.20-1.00mm. Experiments were performed at ambient conditions, with the superficial air velocity ranging from 7.13-9.16m/s, a bed inventory of 7-10 kg, spacing of 0.085 and 0.045 m between the jet top and draft tube bottom, and an operating time of 40h. We investigated the influence of these parameters in terms of changes in the size distribution of particles, changes in the %-weight of particles of different size ranges, generation of particles with smaller diameters, the decrease of the downcomer bed height, variations in the coefficient of uniformity and coefficient of curvature, and material loss from entrainment of fines with increasing operation time. The mode of attrition was abrasion in all experiments. We found that with increasing operation time and other parameters (bed inventory, superficial air velocity, and spacer height) attrition of the bed material also increased. Generation and elutriation of fines were more pronounced at higher superficial air velocity, bed inventory, and spacer height. (C) 2017 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:61 / 70
页数:10
相关论文
共 39 条
[1]  
Alappat BJ, 1996, INT J ENERG RES, V20, P313
[2]   Performance prediction of an RCFB incineration system [J].
Alappat, BJ ;
Rane, VC .
JOURNAL OF ENERGY ENGINEERING-ASCE, 2000, 126 (02) :53-65
[3]   Solid circulation rate in recirculating fluidized bed [J].
Alappat, BJ ;
Rane, VC .
JOURNAL OF ENERGY ENGINEERING-ASCE, 2001, 127 (02) :51-68
[4]  
[Anonymous], AM I CHEM ENG S SERI
[5]   A REVIEW OF ATTRITION AND ATTRITION TEST METHODS [J].
BEMROSE, CR ;
BRIDGWATER, J .
POWDER TECHNOLOGY, 1987, 49 (02) :97-126
[6]   SOLIDS CIRCULATION IN A SPOUT FLUID BED WITH DRAFT TUBE [J].
BERRUTI, F ;
MUIR, JR ;
BEHIE, LA .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1988, 66 (06) :919-923
[7]   A review of attrition of fluid cracking catalyst particles [J].
Boerefijn, R ;
Gudde, NJ ;
Ghadiri, M .
ADVANCED POWDER TECHNOLOGY, 2000, 11 (02) :145-174
[8]   Pressure drop and gas bypassing in recirculating fluidized beds [J].
Chandel, MK ;
Alappat, BJ .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (05) :1489-1499
[9]   Limestone particle attrition and size distribution in a small circulating fluidized bed [J].
Chen, Zhongxiang ;
Grace, John R. ;
Lim, C. Jim .
FUEL, 2008, 87 (07) :1360-1371
[10]   Development of particle size distribution during limestone impact attrition [J].
Chen, Zhongxiang ;
Grace, John R. ;
Lim, C. Jim .
POWDER TECHNOLOGY, 2011, 207 (1-3) :55-64