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
  • [1] REACTOR DEVELOPMENT FOR THE ULTRAPYROLYSIS PROCESS
    BERG, DA
    BRIENS, CL
    BERGOUGNOU, MA
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1989, 67 (01) : 96 - 101
  • [2] STATIC INSTABILITY ANALYSIS OF CIRCULATING FLUIDIZED-BEDS AND CONCEPT OF HIGH-DENSITY RISERS
    BI, HT
    ZHU, JX
    [J]. AICHE JOURNAL, 1993, 39 (08) : 1272 - 1280
  • [3] Modeling circulating fluidized bed downers
    Bolkan, Y
    Berruti, F
    Zhu, J
    Milne, B
    [J]. POWDER TECHNOLOGY, 2003, 132 (2-3) : 85 - 100
  • [4] COMPUTER-SIMULATION OF THE PERFORMANCE OF FLUID CATALYTIC CRACKING RISERS AND DOWNERS
    BOLKANKENNY, YG
    PUGSLEY, TS
    BERRUTI, F
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (12) : 3043 - 3052
  • [5] Characterization of downflowing high velocity fluidized beds
    Cao, CS
    Weinstein, H
    [J]. AICHE JOURNAL, 2000, 46 (03) : 515 - 522
  • [6] [陈恒志 Chen Hengzhi], 2002, [过程工程学报, The chinese journal of process engineering], V2, P186
  • [7] Experimental study of the deep catalytic cracking process in a downer reactor
    Deng, RS
    Wei, F
    Jin, Y
    Zhang, QH
    Jin, Y
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (24) : 6015 - 6019
  • [8] Situating the high-density circulating fluidized bed
    Grace, JR
    Issangya, AS
    Bai, DR
    Bi, HT
    Zhu, JX
    [J]. AICHE JOURNAL, 1999, 45 (10) : 2108 - 2116
  • [9] Flow study of a 0.05 m diameter downflow circulating fluidized bed
    Herbert, PM
    Gauthier, TA
    Briens, CL
    Bergougnou, MA
    [J]. POWDER TECHNOLOGY, 1998, 96 (03) : 255 - 261
  • [10] Bed-to-wall heat transfer in a downer reactor
    Kim, YJ
    Bang, JH
    Kim, SD
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (02) : 207 - 212