期刊文献+

球团竖炉结构影响炉内气流分布的实验研究 被引量:7

Experimental Study on Gas Flow Distribution Affected by Constructional Parameters of Pelletizing Shaft Furnaces
下载PDF
导出
摘要 根据相似原理建立了球团竖炉冷态模型实验台,依据实验数据绘制流网图,通过流网图判断炉内气流运动,从而得到竖炉结构参数对气流分布的影响规律·结果表明,结构参数中,导风墙宽、焙烧带宽、冷却带宽、焙烧带高、均热带高和冷却带高等是影响气流分布的主要因素,其中,导风墙宽增大,或焙烧带宽减小,或火口中心线上料层增高,则上行冷却风趋势减小,下行焙烧风趋势增大,临界流入风量比k 减小;反之,上行冷却风趋势增大,下行焙烧风趋势减小,k 增大;此外,焙烧带宽是影响气流分布均匀性的主要因素·此研究结果可指导竖炉的初始设计和生产参考,尤其供竖炉的计算机辅助设计参考· Pelletizing shaft furnace(PSF) is usually used to produce acidic pellet in China. A cold-state experimental set-up was built according to the principle of similitude, and then the flow-net diagrams with different constructional parameters were plotted to make sure of the gas flow distribution in PSF and how the gas flow distribution is affected by the constructional parameters. The results showed that among such constructional parameters the widths of vertical air internal channels, roasting zone and cooling zone and the heights of roasting zone, soaking zone and cooling zone are the main influencing factors on gas flow distribution in PSF. In case the width of internal channels or the height of roasting zone is increased or the width of roasting zone decreased, the upward cooling gas tends to decrease while the downward roasting gas tends to increase with the critical ratio of inflow k~* decreased gradually, and vice versa. It is important that the width of roasting zone is the key influencing factor on the uniformity of gas flow distribution in PSF. The results as above can be applied to the initial design of PSF especially in CAD.
出处 《东北工学院学报》 EI CSCD 北大核心 2004年第6期563-566,共4页
基金 国家自然科学基金资助项目(50334020) 国家重点基础研究规划项目(2000026300)
关键词 球团竖炉 气流分布 相似原理 填料床 固定床 冶金炉 pellet shaft furnace packed bed fixed bed metallurgical furnace gas/fluid flow
  • 相关文献

参考文献10

  • 1孔令坛.中国炼铁原料技术的科技进步和展望[J].中国冶金,2003,13(4):1-4. 被引量:20
  • 2董辉,蔡九菊,王国胜,田红.球团竖炉内气流运动规律的实验研究[J].东北大学学报(自然科学版),2004,25(5):435-438. 被引量:15
  • 3Paterson W R, Berresford E J. Gas flow maldistribution in moving beds of monosized particles [ J ]. Chem Fluid Sci,2000,55 (17) :3515 - 3527.
  • 4Sodr J R. Fluid flow pressure drop through an annular bed of spheres with wall effects[J]. Therm fluid Sci, 1998, 17(3) :265-275.
  • 5Stanek, 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.
  • 6Achenbach E. Heat and transfer characteristics of packed beds[J]. Experimental Thermal and Fluid Science, 1998,10:17-27.
  • 7Amiri A, Vafai K. Transient analysis of incompressible flow through a packed bed[J ]. International Journal of Heat and Mass Transfer, 1998,41:4259- 4279.
  • 8Stank 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.
  • 9Moise A, Tudose R Z. Air isothermal flow through packed beds[J ]. Experimental Thermal and Fluid Science, 1998,18:134- 141.
  • 10John E F, Joseph B F. Fluid mechanics with engineering applications [ M ]. Beijing: Tsinghua University Press,2003. 193- 198,629- 630.

二级参考文献11

  • 1A.H.拉姆.现代高炉过程的计算分析[M].北京:冶金工业出版社,1987,11..
  • 2张一敏.球团理论与工艺[M].北京:冶金工业出版社,2002.31.
  • 3东北工学院冶金炉教研室.冶金炉理论基础[M].北京:中国工业出版社,1962..
  • 4Negrini A I, Freire J T. Fluid dynamics of air in a packed bed: velocity profiles and the continuum model assumption[J]. Brazil J Chem Eng, 1999,16(4):421-432.
  • 5Paterson W R, Berresford E J. Gas flow maldistribution in moving beds of monosized particles [ J ]. Chem Fluid Sci,2000,55(17) :3515 - 3527.
  • 6Sock J R. Fluid flow pressure drop through an annular bed of spheres with wall effects[J]. Therm Fluid Sci, 1998, 17(3) :265 - 275.
  • 7Stanek, Vladimir, Jircny. Experimental observation of pressure drop oversH∞t following an onset of gas flow in counter-current beds[J ]. Chem Eng J, 1997,68(2 - 3):207 - 210.
  • 8Yin F H, Wang Z C. Experimental studies of liquid flow maldistribution in a random packed columns[J ]. Can J Chem Eng, 2000,78(3) :449 - 457.
  • 9Stank 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.
  • 10Stank V, Szekely J. Three-dimensional flow of fluids through non-uniform packed beds[J ]. A I Che J, 1974,20 (5): 597- 980.

共引文献31

同被引文献206

引证文献7

二级引证文献21

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