期刊文献+

球团竖炉结构参数影响炉内气体流动的数值模拟 被引量:2

Numerical Simulation on Gas Flow Affected by Constructional Parameters of Pelletizing Shaft Furnaces
下载PDF
导出
摘要 运用气固填料床动力学理论建立了球团竖炉料层内气体流动的数学模型,确立了数学模型的边界条件.运用手编程模拟研究炉内气体流动的基本规律,进而探讨竖炉结构参数对炉内气体流动的影响.结果表明:结构参数中,导风墙宽度、焙烧带宽度以及预热焙烧带高度是影响炉内气体流动的主要因素.导风墙宽度和预热焙烧带高度的增加,以及焙烧带宽度的减小会导致冷却风上行趋势减小,焙烧风下行趋势增大.同时,导风墙宽度、预热焙烧带高度以及焙烧带宽度的改变也会导致竖炉内焙烧风与冷却风之比发生改变,即流入风量比发生改变,而流入风量比是决定炉内气体流动的最主要因素. According to the gas solid packed bed dynamic theory,the mathematical model of the gas flow in the pellet shaft furnace(PSF) layer was established,and the boundary conditions of the mathematical model were determined.The basic law of the gas flow in PSF was studied by using the manual programming simulation,further more the influences of the structural parameters of PSF on the gas flow were discussed.The results showed that in the structural parameters,the width of the internal vertical air channels and roasting zone,the height of preheating roasting zone were the major factors that influenced the gas flow in PSF.With the increase of the width of internal vertical air channels or the height of preheating roasting zone and the decrease of the width of roasting zone,the upward cooling gas flow tended to decrease,while the downward roasting gas tended to increase.At the same time,the change of the width of internal vertical air channels or the roasting zone and the height of preheating roasting zone,also led to the change of the ratio of the roasting gas and the cooling gas,namely the change of the ratio of air volume,which was the main factor to decide the gas flow in PSF.
出处 《东北大学学报(自然科学版)》 EI CAS CSCD 北大核心 2013年第7期980-984,共5页 Journal of Northeastern University(Natural Science)
基金 国家自然科学基金资助项目(51274065)
关键词 填料床 球团竖炉 气体流动 结构参数 数值模拟 packed bed pelletizing shaft furnace gas flow structural parameters numerical simulation
  • 相关文献

参考文献9

  • 1董辉,蔡九菊,王国胜,杨俊.球团竖炉内气体流动的数值模拟[J].东北大学学报(自然科学版),2006,27(5):509-512. 被引量:6
  • 2Negrini A I,Freire J T. Fluid dynamics of air in a packedbed : velocity profiles and the continuum model assumption[J ]. Brazilian Journal of Chemical Engineering, 1999,16(4):421 -432.
  • 3Paterson W R,Berresford E J. Gas flow distribution inmoving beds of monosized particles [ J ]. ChemicalEngineering Science ,2000,55 (17) :3515 -3527.
  • 4Yin F H,Wang Z C. Experimental studies of liquid flowdistribution in a random packed columns [ J ]. CanadianJournal of Chemical Engineering ,2000,78 (3) :449 -457.
  • 5Moise A,Tudose R Z. Air isothermal flow through packedbeds[ J]. Experimental Thermal and Fluid Science ,199^, 18(3):134-141.
  • 6董辉,蔡九菊,王国胜,傅巍.球团竖炉结构影响炉内气流分布的实验研究[J].东北工学院学报,2004,25(6):563-566. 被引量:7
  • 7Finnemore E J,Franzini J B.流体力学及其工程应用[M].北京:清华大学出版社,2003.
  • 8Stank V, Szekely J. The effect of non-uniform porosity incausing flow maldistribution in isothermal packed beds[ J].Canadian Journal of Chemical Engineering ,1973,51(3) :22-30.
  • 9Kincaid D, Cheney W. Numerical analysis: mathematics ofscientific computing [ M ]. 3rd ed. San Diego : AmericanMathematical Society ,2003 :572 -596.

二级参考文献18

  • 1李蒙,任伟,陈三凤.国内外球团矿生产现状和展望[J].中国冶金,2004,14(11):1-3. 被引量:13
  • 2Amiri A, Vafai K. Transient analysis of incompressible flow through a packed bed[J ]. International Journal of Heat and Mass Transfer, 1998,41:4259- 4279.
  • 3Stank V, Szekely J. The effect of non-uniform porosity in causing flow maldistribution in isothermal packed beds[J ].Can J Chem Eng, 1973,51(3):22-30.
  • 4Moise A, Tudose R Z. Air isothermal flow through packed beds[J ]. Experimental Thermal and Fluid Science, 1998,18:134- 141.
  • 5John E F, Joseph B F. Fluid mechanics with engineering applications [ M ]. Beijing: Tsinghua University Press,2003. 193- 198,629- 630.
  • 6Paterson W R, Berresford E J. Gas flow maldistribution in moving beds of monosized particles [ J ]. Chem Fluid Sci,2000,55 (17) :3515 - 3527.
  • 7Sodr J R. Fluid flow pressure drop through an annular bed of spheres with wall effects[J]. Therm fluid Sci, 1998, 17(3) :265-275.
  • 8Stanek, Vladimir, Jircny. Experimental olxservation of pressure drop overshoot following an on.set of gas flow in counter-current beds[J]. Chem Eng J, 1997,68(2-3):207-210.
  • 9Achenbach E. Heat and transfer characteristics of packed beds[J]. Experimental Thermal and Fluid Science, 1998,10:17-27.
  • 10Ergun S.Fluid flow through packed columns[J].Chemical Engineering Progress,1952,48(2):89-94.

共引文献9

同被引文献11

引证文献2

二级引证文献1

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