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磷矿颗粒流态化特性的实验研究 被引量:4

Experimental study on fluidization characteristics of phosphate ore particles
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摘要 在高1 m、内径42 mm的流化床中,对粒径54—600μm、密度2 252—2 665 kg/m3的磷矿颗粒的流态化特性进行实验研究。实验结果表明:磷矿颗粒粒径和密度对磷矿颗粒流态化行为有较大影响,床层膨胀比随着磷矿颗粒粒径的增大而逐渐减小。当磷矿颗粒属于Geldart B类颗粒时,流化较好;而当颗粒平均粒径为82μm时,虽然属于A类颗粒,但由于颗粒间力较大,不易流化,出现柱塞状上升、沟流等不正常流化现象,表现出拟C类颗粒的流态化特性。通过测量床层压降,获得了磷矿颗粒的最小流化速度,并与不同的最小流化速度关联式的计算结果进行比较,计算结果显示Thonglimp关联式对B类颗粒更符合实验结果,并提出了适合磷矿颗粒的最小流化速度的关联式。 The fluidization characteristics of phosphate ore particles with sizes varying from 54 to 600 μm and densities of 2 252-2 665 kg/m3 were experimentally investigated in a fluidized bed of 1 m in height and 42 mm in interior diameter. The results indicate that the fluidization behaviors of phosphate ore particles strongly depend on their densities and mean sizes. The bed expansion ratio of the particles decreases with increasing mean sizes. The phosphate ore particles belonging to Geldart B can be fluidized smoothly. However, the particles in the mean size of 82 p^n, belonging to Geldart A, are difficult to be fluidized, similar to the flnidization behavior of Geldart C. Iarge interparticle forces lead to plugging and channeling. The experimental values of minimum fluidization velocity were obtained by measuring the pressure drop across the bed. Several classical correlations were used to fit the experimental data of minimum flnidization velocity, and Thonglimp correlation for Geldart B agrees reasonably with the experimental data. A new correlation in explicit form was developed for better model of the minimum fluidization velocity.
出处 《化学工程》 CAS CSCD 北大核心 2011年第12期69-72,99,共5页 Chemical Engineering(China)
基金 国家科技支撑计划项目(2007BAB08B10) 教育部"矿物处理过程强化"创新团队资助项目(IRT0974)
关键词 流态化 磷矿 最小流化速度 磷酸 窑法磷酸 fluidization phosphate ore minimum fluidization velocity phosphoric acid kiln phosphoric acid process
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参考文献13

  • 1MEGY J A, HARD R A. Process for producing phosphorus pentoxide or phosphorus or phosphoric acid: US, 4351813[P]. 1982-09-28.
  • 2田昊一,康明雄,刘根炎,吴元欣,杜志平,袁华.我国磷酸生产工艺分析与展望[J].化工矿物与加工,2011,40(1):1-5. 被引量:26
  • 3YANG Wen-Ching. Handbook of fluidization and fluid-particle systems [M]. New York: Marcel Dekker, 2003.
  • 4GELDART D. Types of gas fluidization [ J ]. Powder Technol, 1973,7 (5) :285-292.
  • 5WEN C Y, YU Y H. A generalized method for predicting the minimum fluidization velocity [ J ]. AIChE J, 1966, 12(3) :610-612.
  • 6BABU S P, SHAH B, TALWALKER A. Fluidization correlations for coal gasification materials-minimum fluidization velocity and fluidized bed expansion ratio [ J ].Chemical Engineering Progress Symposium Series, 1978, 74(16) :176-186.
  • 7BOURGEOIS P, GRENIER P. Ratio of terminal velocity to minimum fluidization velocity for spherical particles [J]. Can J Chem Eng, 1968,46(5) :325-328.
  • 8RICHARDSON J F, JEROMINO M A D S. Velocity voidage relations for sedimentation and tluidization [ J ]. Chem Eng Sci, 1979,34(16) :1419-1422.
  • 9SAXENA S C, VOGEL G J. The measurement of incipient fluidization velocities in a bed of course dolomite at temperature and pressure [ J ]. Trans Int Chem Eng, 1977,55(6) : 184-189.
  • 10CHITESTER D C, KORNOSKY R M, FAN L S, et al. Characteristics of fluidization at high pressure [ J ]. Chem Eng Sci, 1984,39(2) :253-261.

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同被引文献23

  • 1侯拥和.磷矿石中脉石成分对窑法磷酸工艺的影响[J].矿冶工程,1993,13(3):49-54. 被引量:4
  • 2郭慕孙.流态化手册[M].北京:化学工业出版社,2007.
  • 3Geldart D. Types of gas fluidization [J]. Powder Technol, 1973,7(5): 285 - 292.
  • 4Leder F, Park W C, Chang P W. New process for technical-grade phos- phoric acid [J]. Ind Eng Chem Process Des Dev, 1985, 24(3): 688- 697.
  • 5Richardson J F, Zaki W N. Sedimentation and fluidisation: Part I [J]. Transactions of the Institute of Chemical Engineers, 1954, 3(2): 35-53.
  • 6LEDER F,PARK W C, CHANG P W, et al. New process for technical-grade phosphoric acid [ J ]. Ind Eng Chem Process Des Dev,1985,24(3) : 688-697.
  • 7SATHIYAMOORTHY D, HORIO M. On the influence of aspect ratio and distributor in gas fluidized beds [ J ]. Chem Eng J,2003,93(2) :151-161.
  • 8CHYANG C S, LIEU K, HONG S S. The effect of distribu- tor design on gas dispersion in a bubbling fluidized bed [ J]. J Chin Inst Chem Eng,2008,39(6) : 685-692.
  • 9GELDART D. Types of gas fluidization[J]. Powder Techn- ol, 1973, 7(5): 285-292.
  • 10金涌,俞芷青.采用床层塌落技术测量气固流化床浓相空隙率[J].化工学报,1988,(2):137-143.

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