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方形截面循环悬浮床内边角效应的分析 被引量:2

Analyses of Wall and Corner Effects in Square-cross-section Circulating Suspension Beds
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摘要  边角效应是方形或矩形截面的循环悬浮床内气固流动结构的重要特点之一。对于烟气脱硫循环悬浮床,减小边壁颗粒层厚度,使床内颗粒径向分布趋向均匀,会有利于气固接触反应,提高脱硫效率。在方形截面循环悬浮床冷态试验台架上,以空气为流化介质,平均粒径40μm的玻璃珠为循环物料,采用双光路光纤浓度测量系统测定了不同轴向高度截面上的径向颗粒浓度分布,分析了床内构件、表观气速和循环流率对边角效应的影响。研究结果对选择操作条件,尤其是合适的循环流率,以及进一步探索改善床内气固流动结构的方向有参考价值。 Wall and Corner Effects are likly the most important characteristics of gassolid flow configuration in the square or rectangle crosssection circulating suspension beds. For the process of flue gas desulfuration in circulating suspension beds, reducing the thickness or density of wall particle layer, which can lead to uniform radial distribution of particles, is propitious to the contact(reaction) between gas and solid, and can improve the desulphurization efficiency. A cold experimental facility of squarecrosssection circulating suspension bed was used in this work. Air was used as the fluidizing medium, and as the circulating material the glass beads with 40μm meandiameter as. The radial densities of particles were measured in the different cross sections of the bed with a double light fibreoptics density probe. The effects of bed geometry, superficial gas velocity and circulating flow rate on the wall and corner particle layer are analyzed from the demonstration of the thickness and the density's change. It was experimentally found that mounting the separating component, choosing smaller gas superficial velocity and suitable particle circulating flow rate are significant for reducing the thickness or density of the wall particle layer. It would be useful in the further research for improving the gassolid flow structure in the desulfuration circulating suspension bed.
出处 《化学反应工程与工艺》 CAS CSCD 北大核心 2003年第1期56-62,共7页 Chemical Reaction Engineering and Technology
基金 国家重点基础研究专项经费资助(G19990222)
关键词 循环悬浮床 边角效应 表观气速 循环流率 边壁颗粒层 circulating suspension bed wall and corner effect superficial gas velocity circulating flow rate thickness of particle layer
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  • 1黄素华,陆继东,钱诗智,林志杰,刘德昌,伍尉恒.矩形平壁循环流化床冷态流动特性研究[J].热能动力工程,1995,10(3):144-148. 被引量:6
  • 2钱诗智,陆继东,黄素华,林志杰,刘德昌.循环流化床壁面的几何结构对床层气固流动特性的影响[J].化工学报,1996,47(6):706-711. 被引量:6
  • 3董元吉 李静海 等.快速流化床径向空隙率分布测定及关联[J].化学反应工程和工艺,1988,4(1):75-81.
  • 4Zheng C G, Tung Y G , Xia Y S, et al. Internals for Fast Fluidized Beds. in: Kwauk M, Hasatani. Fluidization'91 Science and Technology. Beijing: Science Press. 1991. 413~416.
  • 5Wei F. Zhu J X. Effect of Flow Direction on Axial Solid Dispersion in Gas-Solids Cocurrent Upflow and Downflow Systems. The Chemical Engineering Journal,1996,64(3):345~352.
  • 6Saha A K, Muralidhar K, Biswas G. Vertex Structures and Kinetic Energy Budget in Two Dimensional Flow Past a Square Cylinder. Computers & Fluids, 2000, 29(6) :669~694.
  • 7Der Meer E H van, Thorpe R B, Davidson J F. Flow Patterns in The Square Cross-Section Riser of a Circulating Fuidised Bed and The Elect of Riser Exit Design. Chemical Engineering Science, 2000, 55 (19): 4079~4099.
  • 8Zhu J X, Salah M, Zhou Y. Radial and Axial Voidage Distributions in Circulating Fluidized Bed with Ring-Type Internals. Chemical Engineering Journal of Japan,1997, 30(5) :928~937.
  • 9Zhong W Q,Zhang M Y,Jin B S,et al.Experimental Investigation of Particle Mixing Behavior in a Large Spout-fluidized Bed. Chem.Eng.Process . 2007
  • 10J. Zhou,J. R. Grace S. Qin C. M. H. Brereton,C. J. Lim and J. Zhu.Voidage profiles in a circulating fluidized bed of square cross-section. Chemical Engineering Science . 1994

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