Characterization of a high-density downer reactor

被引:26
作者
Chen, HZ [1 ]
Li, HZ [1 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, Multiphase React Lab, Beijing 100080, Peoples R China
基金
中国国家自然科学基金;
关键词
high-density downer; solids flux; transient solids concentration; solids concentration distribution;
D O I
10.1016/j.powtec.2004.07.008
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Experiments were carried out in a specially designed circulating fluidized bed with a 5.6-m tall, 0.08 m ID downer, in which the maximal the solids flux 600 kg m(-2) s(-1) and the maximal solids holdup 0.14 have been achieved. The results show that single peak exists in the PDD curves of the solids concentration for low-density operation, and a higher platform is present in the PDD curves for the high-density downer. Solids flux is a key factor that affects the solids holdup while particle properties are other important parameter. The heavier/better fluidity particle could achieve the structure still exists in the high-density downer, but radial solids distribution gradually becomes more uniform with downward distance and with the increase of solids flux. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:84 / 92
页数:9
相关论文
共 22 条
  • [11] Coal gasification characteristics in a downer reactor
    Kim, YJ
    Lee, SH
    Kim, SD
    [J]. FUEL, 2001, 80 (13) : 1915 - 1922
  • [12] Characterization of the flow pattern in a downer reactor
    Lehner, P
    Wirth, KE
    [J]. CHEMICAL ENGINEERING SCIENCE, 1999, 54 (22) : 5471 - 5483
  • [13] Effects of the gas solids distributor on the local and overall solids distribution in a downer reactor
    Lehner, P
    Wirth, KE
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (02) : 199 - 206
  • [14] Characterization of high-density gas-solids downward fluidized flow
    Liu, W
    Luo, KB
    Zhu, JX
    Beeckmans, JM
    [J]. POWDER TECHNOLOGY, 2001, 115 (01) : 27 - 35
  • [15] Experimental study of heat transfer in a co-current downflow fluidized bed (downer)
    Ma, Y
    Zhu, JX
    [J]. CHEMICAL ENGINEERING SCIENCE, 1999, 54 (01) : 41 - 50
  • [16] An experimental study on gasification of Colombian coal in fluidised bed
    Ocampo, A
    Arenas, E
    Chejne, F
    Espinel, J
    Londoño, C
    Aguirre, J
    Perez, JD
    [J]. FUEL, 2003, 82 (02) : 161 - 164
  • [17] Development of a downer reactor for fluid catalytic cracking
    Talman, JA
    Geier, R
    Reh, L
    [J]. CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) : 2123 - 2130
  • [18] Transient dynamics of solid concentration in downer fluidized bed
    Tuzla, K
    Sharma, AK
    Chen, JC
    Schiewe, T
    Wirth, KE
    Molerus, O
    [J]. POWDER TECHNOLOGY, 1998, 100 (2-3) : 166 - 172
  • [19] Hydrodynamics in downflow fluidized beds (1): solids concentration profiles and pressure gradient distributions
    Zhang, H
    Zhu, JX
    Bergougnou, MA
    [J]. CHEMICAL ENGINEERING SCIENCE, 1999, 54 (22) : 5461 - 5470
  • [20] Gas-solids flow behavior: CFB Riser vs. Downer
    Zhang, H
    Huang, WX
    Zhu, JX
    [J]. AICHE JOURNAL, 2001, 47 (09) : 2000 - 2011