期刊文献+

炭素回转窑内物料停留时间的确定 被引量:2

Calculation of Mean Residence Time of Solids in Carbon Rotary Kilns
下载PDF
导出
摘要 在前人建立的等径回转窑内物料料层轴向厚度变化公式基础上,推导出了适合于窑尾扩径和内衬增设翻料装置的变径窑内物料层厚度的计算式;同时利用上述两种窑内料层厚度计算式进一步求出了两种窑内物料停留时间的计算式,计算式中综合考虑了窑内径、窑长、窑头挡料圈高度、窑倾角、窑转速、物料体积流率、物料安息角、物料颗粒粒径等多种因素;为了验证计算公式的正确性,建立了实验装置,进行了冷态实验测试.结果表明,公式计算值与实验测试值比较吻合,误差较小,并且计算中不需要引入修正系数. Based on the earlier works concerning the formula of the change in the axial depth of a bed in a diameter-invariable rotary kiln,the formula of axial depth of bed in a diameter-variable kiln was deduced to adapt to the diameter enlargement at kiln inlet and the turn-down rigs set on the kiln lining.Then,the formulae of mean residence time of solids in both diameter-invariable and diameter-variable kilns were deduced,where several factors were taken into account,such as the inner diameter,total length,discharge dam height,axis inclination and rotation speed of kiln mass feed rate of solids,and the particle diameter and dynamic angle of repose of solids.Cold-state experiments were carried out on a laboratory rotary kiln to verify the formulae proposed,and the results showed that calculated results of the residence time of solids are basically in agreement with the experimental values,with no correction coefficient required beause of small errors.
出处 《东北大学学报(自然科学版)》 EI CAS CSCD 北大核心 2010年第9期1313-1317,共5页 Journal of Northeastern University(Natural Science)
基金 国家科技支撑计划项目(2006BAB12B04)
关键词 炭素回转窑 等径窑 窑尾扩径 翻料装置 物料停留时间 carbon rotary kiln diameter-invariable kiln diameter enlargement at kiln inlet turn-down rigs residence time of solids
  • 相关文献

参考文献8

  • 1Liu X Y, Specht E. Mean residence time and hold-up of solids in rotary kilns[J].Chemical Engineering Science, 2006,61 (15) :5176 - 5181.
  • 2Chatterjee A, Sathe A V, Mukhopadhyay P K. Flow of materials in rotary kilns used for sponge iron manufacture: part II. effect of kiln geometry[J].Metallurgical and Materials Transactions 13, 1983,14(3) :383 - 392.
  • 3Li S Q, Yan J H, Li R D, et al. Axial transport and residence time of MSW in rotary kilns: part I. experimental [J]. Powder Technology, 2002,126(3) :217 - 227.
  • 4Li S Q, Chi Y, Li R D, et al. Axial transport and residence time of MSW in rotary kilns: part II . theoretical and optimal analysis[J]. Pozvder Technology, 2002,126(3) :228 - 240.
  • 5Saernan W C. Passage of solids through rotary kilns: factors affecting time of passage[J]. Chemical Engineering Progress, 1951,47(10) :508 - 514.
  • 6Kramers H, Croockewit P. The passage of granular solids through inclined rotary kilns [ J ]. Chemical Engineering Science, 1952,1(6) :259 -265.
  • 7Spurling R J, Davidson J F, Scott D M. The no-flow problem for granular material in rotating kilns and dish granulators[J]. Chemical Engineering Science, 2000,55(12):2303- 2313.
  • 8Labas E, Houzelot J L, Ablitzer D, et al. Experimental study of residence time, particle movement and bed depth profile in rotary kilns[J]. Canadian Journal of Chemical Engineering, 1995,73(2) : 173 - 180.

同被引文献41

  • 1JAVEN T, JIE B, NICOLAS H, YANG R Y. Modeling collective dynamics of particulate systems under time-varying operating conditions based on Markov chains[J]. Advanced Powder Technology, 2013, 24(2): 451-458.
  • 2MELLMANN J. The transverse motion of solids in rotating cylinders-forms of motion and transition behavior[J]. Powder Technology, 2001, 118(3): 251-270.
  • 3KHAKHAR D V, MCCARTHY J J, TROY SHINBROT, OTT1NO J M. Transverse flow and mixing of granular materials in a rotating cylinder[J]. Phys Fluids, 1997, 9(1): 31-43.
  • 4NIELSEN A R, ANIOL R W, LARSEN M B, GLARBORG P. Mixing large and small particles in a pilot scale rotary kiln[J]. Powder Technology, 2011, 210(3): 273-280.
  • 5van PUYVELDE D R, YONG B R, WILSON M A. Experiment determination of transverse mixing kinetics in a rolling drum by image analysis [J]. Powder Technology, 1999, 106:183-191.
  • 6van PUYVELDE D R. Comparison of discrete elemental modelling to experimental data regarding mixing of solids in the transverse direction of a rotating kiln[J]. Chemical Engineering Science, 2006, 61: 4462-4465.
  • 7SCHUTYER M A I, PADDING J T, WEBER F J. Discrete particle simulation predicting mixing behavior of solid substrate particles in a rotating drum fermenter[J]. Biotechnology and Bioengineering, 2001, 75(6): 665-675.
  • 8FINNIE G J, KRUYT N P, YE M. Longitudinal and transverse mixing in rotary kilns: A discrete element method approach[J]. Chemical Engineering Science, 2005, 60:4083-4091.
  • 9LIU P Y, YANG R Y, YU A B. DEM study of the transverse mixing of wet particles in rotating drums[J]. Chemical Engineering Science, 2013, 86: 99-107.
  • 10DOUCET J, BERTRAND F, CHAOUKI J. An extended radioactive particle tracking method for systems with irregular moving boundaries[J]. Powder Technology, 2008, 181(2): 195-204.

引证文献2

二级引证文献19

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