CIESC Journal

• Original Article • 上一篇    下一篇

THE PARTICLE VELOCITY DISTRIBUTION IN A RISER OF DILUTE CIRCULATING FLUIDIZED BED

杨勇林; 金涌; 俞芷青; 汪展文; 白丁荣   

  1. Dept. of Chem. Eng., Tsinghua University, Beijing
  • 收稿日期:1990-06-03 修回日期:1990-10-11 出版日期:1991-12-28 发布日期:1991-12-28
  • 通讯作者: 杨勇林

THE PARTICLE VELOCITY DISTRIBUTION IN A RISER OF DILUTE CIRCULATING FLUIDIZED BED

YANG Yonglin; JIN Yong; YU Zhiqing; WANG Zhanwen; BAI Dingrong   

  1. Dept. of Chem. Eng., Tsinghua University, Beijing
  • Received:1990-06-03 Revised:1990-10-11 Online:1991-12-28 Published:1991-12-28
  • Contact: YANG Yonglin

摘要: This paper presents an experimental study on the radial and axial profiles of local particle velocity of flu-idized catalyst(FCC)particles in a circulating fluidized bed of 8000mm in height and 186mm in inside diameterwith a Fiber-Optic Probe Laser Doppler Velocimetry.It has been found that the radial profiles of local particlevelocity are parabolic,even in the centre region and steep in the region near the bed wall,and that the length ofparticle acceleration along the bed height is longer than expected.The following formula has been recommended to correlate the 1 ocal particle velocity with dilute gas-solidflow in the bed:where a,b,c and e are functions of radial positions.

Abstract: This paper presents an experimental study on the radial and axial profiles of local particle velocity of flu-idized catalyst(FCC)particles in a circulating fluidized bed of 8000mm in height and 186mm in inside diameterwith a Fiber-Optic Probe Laser Doppler Velocimetry.It has been found that the radial profiles of local particlevelocity are parabolic,even in the centre region and steep in the region near the bed wall,and that the length ofparticle acceleration along the bed height is longer than expected.The following formula has been recommended to correlate the 1 ocal particle velocity with dilute gas-solidflow in the bed:where a,b,c and e are functions of radial positions.