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›› 2012, Vol. 12 ›› Issue (3): 376-381.

• 流动与传递 • 上一篇    下一篇

气固逆流下行流化床中颗粒速度的径向与轴向分布

李正杰 董鹏飞 宋文立 范垂钢 李松庚 林伟刚   

  1. 中国科学院过程工程研究所多相复杂系统国家重点实验室 中国科学院过程工程研究所多相复杂系统国家重点实验室 中国科学院过程工程研究所多相反应实验室 中国科学院过程工程研究所多相反应实验室 中国科学院过程工程研究所多相反应实验室，北京 100080 中国科学院过程工程研究所多相反应开放实验室
  • 收稿日期:2012-03-23 修回日期:2012-04-19 出版日期:2012-06-20 发布日期:2012-06-20
  • 通讯作者: 李正杰

Radial and Axial Distributions of Particle Velocity in a Counter-current Fluidized Bed

LI Zheng-jie DONG Peng-fei SONG Wen-li FAN Chui-gang LI Song-geng LIN Wei-gang   

  1. State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, CAS State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, CAS Institute of Process Engineering, CAS Multi-phase Reaction Laboratory, Institute of Process Engineering Chinese Academic of Science Multi-phase Reaction Laboratory, Institute of Process Engineering, Chinese Academy of Sciences Multi-phase Reaction Laboratory, Institute of Process Engineering Chinese Academic of Science
  • Received:2012-03-23 Revised:2012-04-19 Online:2012-06-20 Published:2012-06-20
  • Contact: LI Zheng-jie

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摘要： 在内径90 mm、高7 m的逆流下行床冷态实验装置中，研究了气固逆流下行床中循环锅炉灰(dp=300 mm)颗粒速度的径向分布及其沿轴向发展. 结果表明，局部颗粒速度沿径向分布是不均匀的，在完全发展区，颗粒速度中心和边壁低、在r/R=0.85附近颗粒速度最大. 由大量实验数据回归出预测充分发展段局部颗粒速度的关联式，该公式计算值与实验值的平均相对偏差小于±11%. 不同径向位置的局部颗粒速度沿轴向的变化趋势不同，边壁区域(r/R>0.622)颗粒速度沿轴向单调递增，而中心区域(0

关键词: 逆流, 下行床, 循环锅炉灰, 颗粒速度, 径向分布, 轴向分布

Abstract: Experiments were carried out in a 90 mm i.d., 7 m high gas upflow and solid downflow fluidized with circulating boiler ash (dp=300 mm) to measure the radial profiles of particle velocity and concentration, and its axial development. The results show that particle velocity is lower both in the center and near the wall in the fully developed region. The maximum particle velocity exists at around r/R=0.85. An empirical formula of particle velocity in the developed region is derived from a number of experimental data. Relative errors between calculated values and experiential data are less than ±11%. Local particle velocity in the region near the bed wall (r/R>0.622) increases along the column. While local particle velocity in the central region (0

Key words: countercurrent, downer, circulating boiler ash, particle velocity, radial profile, axial profile

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