期刊文献+

狭缝式矩形喷动床中多粒度颗粒体系的最小喷动速度 被引量:6

Minimum Spouting Velocity of Multi-component Particle Mixtures in a Slot-rectangular Spouted Bed
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摘要 在150 mm×50 mm×1100 mm的矩形喷动床中,采用宽度为2, 4, 6 mm 的3种狭缝式气体分布板,研究了单一粒度组成和多粒度组成玻璃珠的最小喷动速度. 实验证明,矩形喷动床的最小喷动速度与物料的粒度和组成有关. 给出了最小喷动速度与颗粒粒径和粒度组成的关联式,作出了多粒度组成颗粒体系最小喷动速度的相图. The minimum spouting velocity of multi-size glass bead mixtures was investigated in a rectangular-slot spouted bed with slot air entry, the width of which varies from 2 mm to 6 mm. The experimental results of single and multi-size particle mixtures show that the minimum spouting velocity of multi-size particles is related with particles diameter and size distribution in the particle mixture. In the present work, the maps of minimum spouting velocity for multi-size particle mixture were obtained, and the empirical relation for minimum velocity Ums was determined to be
出处 《过程工程学报》 CAS CSCD 北大核心 2001年第2期113-116,共4页 The Chinese Journal of Process Engineering
关键词 多粒度颗粒 狭缝式矩形喷动床 最小喷动速度 粒径 slot-rectangular spouted bed multi-size particles minimum spouting velocity
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参考文献5

  • 1毛元夫,颜涌捷.喷动流化床的最小喷动流化速度和床层压降[J].化工冶金,1999,20(2):136-139. 被引量:11
  • 2徐健 王诗凝 等.细颗粒喷动床的喷动特性研究[J].化工冶金,1999,20:166-173.
  • 3《化学工程手册》编辑委员会.化学工程手册-流态化[M].北京:化学工业出版社,1987.186-189.
  • 4徐健,化工冶金,1999年,20卷,增刊,166页
  • 5《化学工程手册》编委会,化学工程手册(流态化),1987年,186页

二级参考文献9

  • 1赵振荣,余嘉耕.喷动-流化床床层压降及其最优化操作探讨[J].化学工程,1994,22(4):42-47. 被引量:4
  • 2国井大藏 列文斯比尔O.流态化工程[M].北京:石油化学工业出版社,1977.214-225.
  • 3巴苏P 弗鲁雷SA.循环流化床锅炉的设计与运行[M].北京:科学出版社,1994..
  • 4铨贤苗 颜涌捷 等.导向管喷动流化床流动特性规律[J].华东理工大学学报,1995,21(4):444-450.
  • 5陈甘棠,流态化技术的理论和应用,1996年,241页
  • 6钱贤苗,华东理工大学学报,1995年,21卷,4期,444页
  • 7岑可法(译),循环流化床锅炉的设计与运行,1994年,273页
  • 8华东石油学院(译),流态化工程,1977年,65页
  • 9毛元夫,陈明强,颜涌捷.连续运转的加压喷动流化床内颗粒停留特性[J].化工冶金,1998,19(2):135-139. 被引量:8

共引文献11

同被引文献53

  • 1徐圣言.喷动床的空气动力学特性及其结构局限性[J].农业机械学报,1996,27(4):130-135. 被引量:10
  • 2徐健 王诗凝 等.细颗粒喷动床的喷动特性研究[J].化工冶金,1999,20:166-173.
  • 3Toshifumi Ishikura,Hiroshi Nagashima,Mitsuharu Ide.Hydrodynamics of a spouted bed with a porous draft tube containing a small amount of finer particles[J].Powder Technology. 2003,131:56-65.
  • 4Muir J R, Berruti F, Behie L A. Solids Circulation in Spouted and Spoutfluid Beds with Draft-tubes [ J]. Chem. Eng.Commun. 1990, 88: 153-171.
  • 5[3]Anabtawi M Z, Minimum Spouting Velocity for Binary Mixture of Particles in Rectangular Spouted Beds[J]. Can. J. Chem.Eng., 1998, 76: 132-136.
  • 6[4]Brunello G, Nina G D, Nunes F C S, et al. Minimum Air Requirments for Spouting Mixed Particles[J]. Can. J. Chem. Eng.,1974, 52: 170-173.
  • 7[5]Ijichi K, Uemura, Y, Hatate, Y, et al. Fluidization of Fine Particles in a Spouted Bed with aDraft-tube[J]. Funtai Kogaku Kaishi/Journal of the Society of Powder Technology, Japan, 1996, 33 (9): 706.
  • 8[6]Xu J, Washizu Y, Nakagawa N, et al. Hold-up of Fine Particles in a Powder-Particle Spouted Bed[J]. Journal of Chemical Engineering of Japan, 1998, 31(1): 61-66.
  • 9[7]Xu J, Osada S, Kato K. Limiting Efficiency for Continuous Drying of Microparticle Slurries in a Powder-Particle Spouted Bed[J]. Journal of Chemical Engineering of Japan, 1998, 31 (1): 35-40
  • 10[8]Wang Sh, Xu J, et al. Gas spouting hydrodynamics of fine particles[J]. Can. J. Chem. Eng., 2000, 78(1 ),156- 160

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