期刊文献+

内循环流化床颗粒流动特性的数值模拟 被引量:4

Numerical Simulation of the Characteristics of Particle Flows in an Internally Circulating Fluidized Bed
在线阅读 下载PDF
导出
摘要 采用离散单元法分析了非均匀布风方式下流化床内的气固流动特性.数值模拟结果表明:床内存在大尺度的颗粒横向循环流动;高风速区为气泡活跃区域,气泡尾涡裹挟颗粒上升是形成内循环的关键环节;供风非均匀程度越大,颗粒内循环力度越强烈;改变风速,颗粒流量变化显著;倾斜布风板设计有利于促进颗粒定向循环过程. Internally circulating fluidized beds play an important role in fields of energy and chemical industry. The hydrodynamics of the gas-solid flow in a fluidized bed with uneven gas supply was studied by using discrete element method (DEM). The results indicate that there are large scale particle circulations in the lateral direction. The analysis shows that the zone with faster gas feed is a bubble active zone, where there is an upward particles stream resulted from the transport of the bubbles, which is thought to be an important factor causing the circulating particle stream in the fluidized column. Moreover, the more uneven the gas is supplied, the more intensive the particle circulation is. And the particle flux is sensitive to the change of the gas velocity. The design of an inclined distributor helps to enhance such directional circulation in the bed.
出处 《上海交通大学学报》 EI CAS CSCD 北大核心 2007年第3期347-351,共5页 Journal of Shanghai Jiaotong University
关键词 内循环流化床 非均匀布风 倾斜布风板 离散单元法 颗粒流量 internally circulating fluidized bed (ICFB) uneven gas supply inclined distributor discrete element method (DEM) particle flux
  • 相关文献

参考文献11

  • 1Freedman W,Davidson J F.Hold up and liquid circulation in bubble columns[J].Transactions of the Institution of Chemical Engineers,1969,47 (3):251-262.
  • 2Merry J M D,Davidson J F.Gulf stream circulation in shallow fluidized bed[J].Transactions of the Institution of Chemical Engineers,1973,51 (4):361-368.
  • 3Limtrakula S,Chalermwattanataia A,Unggurawiroteb K,et al.Discrete particle simulation of solids motion in a gas-solid Fluidized bed[J].Chemical Engineering Science,2003,58:915-921.
  • 4Smith R,Beardmore K,Gras-Mati A.Molecular dynamics simulation of particle-surface interactions[J].Vacuum,1995,46 (8):1195-1199.
  • 5Cundall P A,Strack O D L.A discrete numerical model for granular assemblies[J].Geotechnique,1979,29:47-65.
  • 6Tsuji Y,Kawaguchi T,Tanaka T.Discrete particle simulation of a fluidized bed[J].Powder Technology,1993,77:79-87.
  • 7Hoomans B P B,Kuipers J A M,Briels W J,et al.Discrete particle simulation of bubble and slug formation in a two-dimensional gas-fluidized bed:A hardsphere approach[J].Chemical Engineering Science,1996,51:99-108.
  • 8Xu B H,Yu A B.Numerical simulation of the gassolid flow in a fluidized bed by combining discrete particle method with computation fluid dynamics[J].Chemical Engineering Science,1997,52:2785-2809.
  • 9Wen C Y,Yu Y H.Mechanics of fluidization[J].Chem Engng Prog Symp Ser,1966,62 (5):100-105.
  • 10Gidaspow D.Multiphase flow and fluidization[M].San Diego:Academic Press,1994.

二级参考文献2

共引文献2

同被引文献28

引证文献4

二级引证文献28

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部