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液固循环流化床换热器中固体颗粒分布 被引量:24

Distribution of solid particle in liquid-solid circulating fluidized bed
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摘要 利用CCD图像测量与数据处理系统对多管液固循环流化床换热器中的两相流动特性进行了研究。探讨了下管箱中的分布板结构对固体粒子的体积分数分布、固体粒子的速度分布,以及液固两相流压降的影响。实验结果表明:在循环流化床换热器进口段安装适当结构的多孔板分布器,即多孔板的面积小于床层截面积,且床中心处的遮挡面积大于边缘处的遮挡面积,可以有效地提高固相速度的均匀程度,在较高流速下,能较好地改善固体颗粒在管束中的不均匀分布。 The CCD image measurement and data processing system was used to study two-phase flow properties of multi-pipe circulating fluidized bed. The influence of distributor structure on the holdup and velocity distribution of particles and the pressure drop of the liquid-solid two-phase flow was discussed under the certain height and structure of the inlet and outlet chambers. Experimental results show that the perforated-plate distributors, which are properly arranged in the inlet of chamber of the liquid-solid circulating fluidized bed heat exchanger, with the area of perforated-plate smaller than that of the bed, and the shedding area in the center of the bed larger than that in the edge of the bed, can effectively improve the uniform distribution of the velocity of particles, and decrease the nonuniform distribution of particles in the pipe bundle under high flow rate.
出处 《化学工程》 CAS CSCD 北大核心 2004年第1期17-22,共6页 Chemical Engineering(China)
基金 九五"国家重点科技攻关项目(86 610 21 01)
关键词 液固循环流化床 换热器 固体颗粒分布 粒子分布板 liquid-solid circulating fluidized bed heat exchanger distributor
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参考文献9

  • 1郑传根,董元吉,张文楠,张建国.内部构件对循环流化床颗粒径向分布的影响[J].化工冶金,1990,11(4):296-302. 被引量:7
  • 2潘国昌,郭庆丰,杨伯极.填料塔进料气体分布器的研究[J].炼油设计,1995,25(2):28-32. 被引量:21
  • 3齐世学,宗祥荣,王琳,徐应铨.流化床换热器的研究(Ⅰ)[J].烟台大学学报(自然科学与工程版),1994,7(1):48-54. 被引量:7
  • 4Taborek J. Heat Exchanger: Theory and Practice[ M ]. Washington: Hemisphere publishing Corporation, 1981. 885--896.
  • 5Kollbach J St, Dahm W, Rautenbach R. Continuous cleaning of heat exchanger with reeireulating fluidized bed [J]. Heat Transfer Engineering, 1987, 8 (4):26 --34.
  • 6Raubentach R, Erdmann C, Kollbach J St. The fluidized bed technique in the evaporation of wastewaterswith severe fouling/scaling potential-lasted developments, applications limitations [ J ]. Desalization,1991, 81 (2) : 285--298.
  • 7Zhang L B, Li X L. A study on boiling heat transfer in three-phase circulating fluidized bed [ J ]. Chemical Engineering Journal, 2000, 78 ( 1 ) : 217--223.
  • 8Klaren D G, Bailie R E. The non-fouling fluidized bed heat exchanger [ A ]. Heat Transfer Equipment Fundamentals, Design, Application and Operating Problems[ C ]. New York : American Society of Mechanical Engineer, 1989. 273--279.
  • 9Liang W G, Zhu J X, Yu Z Q, et al. Radial nonuniformity of flow structure in a liquid-solid circulating fluidized bed [ J ]. Chemical Engineering Science, 1996,51 (10) : 2001--2010,.

二级参考文献5

  • 1董元吉,第五届全国流态化会议,1990年
  • 2李静海,化工冶金,1988年,9卷,1期,29页
  • 3董元吉,化学反应工程与工艺,1988年,4卷,1期,75页
  • 4Tung Y,Fluidizaion’ 88-Science and Technology,1988年
  • 5[英]巴特沃思(Butterworth,D·),[英]休伊特(Hewitt,G·) 著,陈学俊等.两相流与传热[M]原子能出版社,1985.

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