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密相输运床径向颗粒体积分数分布的研究 被引量:1

Radical solids volume fraction profiles in dense transport bed
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摘要 在提升管高17 m,内径0.102 m的密相输运床冷态实验装置中,采用B类石英砂颗粒,针对径向颗粒体积分数分布进行了研究。结果表明,径向颗粒体积分数分布不均匀:提升管中心至近壁面附近(r/R=0—0.7),颗粒体积分数较低且基本一致;近壁面处(r/R=0.7—0.9)颗粒体积分数显著升高;壁面附近(r/R=0.9—0.97)达到最大。增加固体循环流率或降低提升管气量,各径向位置颗粒体积分数都增加。其中壁面附近最为明显,提升管中心至近壁面附近变化较小。文中建立了径向颗粒体积分数分布描述关系式,对于A类颗粒和B类颗粒实验结果都能较好地预测。 The radical solids volume fraction profiles were investigated in a dense transport bed (0. 102 m in ID x 17 m in height) with the silica sand belonging to Group B. The results show that the radial solids volume fraction profiles are non-uniform: solids volume fraction is low and almost the same near the riser center ( r/R = 0-0.7 ) ; solids volume fraction increases significantly in the adjacent zone (r/R = 0.7-0.9) ; solids volume fraction becomes the highest near the wall (r/R = 0.9-0.97). As the solids circulation rates increase or the riser air volume decreases, solids volume fraction increases at each radical position. The increase of solids volume fraction is the largest near the wall and relatively small near the riser center. At last, a correlation for predicting radical solids volume fraction profiles was proposed. The predictions of the correlation can work well for both Group A and Group B particles.
出处 《化学工程》 CAS CSCD 北大核心 2013年第1期46-49,共4页 Chemical Engineering(China)
基金 国家高技术研究发展计划项目(863项目)(2006AA05A103) 中国科学知识创新重要方向性项目课题(KGCX2-YW-348)
关键词 密相输运床 气固二相流 径向颗粒体积分数分布 dense transport bed gas-solid two-phase flow radical solids volume fraction profiles
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参考文献9

  • 1肖云汉.以煤气化为基础的多联产技术创新[J].中国煤炭,2008,34(11):11-15. 被引量:9
  • 2肖云汉,徐祥,王岳.粉煤加压密相输运床气化方法及装置:中国,00710063702.4[P].2008-08-13.
  • 3ZHANG W,TUNG Y, JOHNSSON F. Radial voidage pro- files in fast fluidized beds of different diameters [ J ]. Chemical Engineering Science, 1991,46 ( 12 ) : 3045- 3052.
  • 4RHODES M J, ZHOU S, BENKREIRA H. Flow of dilute gas-particle suspensions [ J ]. AIChE Journal, 1992, 38 (12) :1913-1915.
  • 5PATIENCE G S, CHAOUKI J. Solids hydrodynamics in the fully developed region of CFB risers [ C ]//Fluidization V. New York: Engineering Foundation, 1996:33-40.
  • 6ISSANGYA A S, GRACE J R, BAI D R, et al. Radial voidage variation in CFB risers [ J ]. Canadian Journal of Chemical Engineering, 2001,79 ( 2 ) : 279 -286.
  • 7MALCUS S. Experimental modeling study of a high sus- pension density CFB riser[ D ]. New Brunswick:The Uni- versity of New Brunswick,2000 : 234-260.
  • 8ISSANGYA A S. Flow dynamics in high density circulat- ing fluidized bed [ D ]. Vancouver, Canada: The University of British Columbia, 1998 : 112-138.
  • 9GELDART D. Types of gas fluidization [ J ]. Powder Tech- nology, 1973,7 (8) :285-292.

二级参考文献16

  • 1中国统计年鉴2008,国家统计局,2008
  • 2IEA. World Energy Outlook 2006.
  • 3Vision 21 Program Plan - Clean Energy Plants for the 21st Century, Federal Energy Technology Center Office of Fossil Energy. U. S. Department of Energy, 1999.
  • 4Joseph P. Strakey, Vision 21 Advanced Power Plants for the 21st Century, Advanced Coal-Based Power and Environmental System' 98 Conference. Morgantown, WV, 1998.
  • 5Clean Coal Power Initiative. Program Facts, www. netl. doe. gov/coal/ccpi/index. html.
  • 6Topical Report No 21 : Coproduction of Power, Fuels and Chemicaba. U. S. Department of Energy, September 2001.
  • 7FutureGen A Sequestration and Hydrogen Research Initiative. www. netl. doe. gov.
  • 8HYPOGEN Pre- feasibility study final report, January 2005 ,report EUR 21512 EN
  • 9COORETEC, www. cooretec.
  • 10EAGLE Project(coal Energy Application for Gas, Liquid and Electricity), Status of the Project. FutureGen Workshop 2008, February 25, 2008

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