CIESC Journal

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PARTICLE FLOW PATTERNS IN THE RISER AND DOWNER OF CIRCULATING FLUIDIZED BED

杨勇林; 金涌; 俞芷青; 汪展文   

  1. Department of Chemical Engineering, Tsinghua University, Beijing, 100084
  • 收稿日期:1991-08-05 修回日期:1991-11-02 出版日期:1992-12-28 发布日期:1992-12-28
  • 通讯作者: 杨勇林

PARTICLE FLOW PATTERNS IN THE RISER AND DOWNER OF CIRCULATING FLUIDIZED BED

YANG Yonglin; JIN Yong; YU Zhiqing; WANG Zhanwen   

  1. Department of Chemical Engineering, Tsinghua University, Beijing, 100084
  • Received:1991-08-05 Revised:1991-11-02 Online:1992-12-28 Published:1992-12-28
  • Contact: YANG Yonglin

摘要: This paper presents an experimental study on the flow patterns of FCC particles in a 140 mm ID Circulating Fluidized Bed with concurrent upflow and downflow gas-solid suspension. Based on the distribution of local particle velocity and particle concentration measured by a Fiber-Optical Probe Laser Doppler Velocimeter and a Fiber Optical Probe System respectively, the different flow patterns of local particls concentration, local particle velocity, local particle fluctuating velocity and sectionally average particle velocity in concurrent upflow and downflow gas-solid system have been investigated. It is found that the particle flow in the concurrent downflow is much more uniform radially than that in the concurrent upflow riser. The investigation of flow patterns in different flow systems is of significance to the development of a new gas-solid reactor.

关键词: particle velocity;particle concentration;flow pattern;riser;downer and LOV

Abstract: This paper presents an experimental study on the flow patterns of FCC particles in a 140 mm ID Circulating Fluidized Bed with concurrent upflow and downflow gas-solid suspension. Based on the distribution of local particle velocity and particle concentration measured by a Fiber-Optical Probe Laser Doppler Velocimeter and a Fiber Optical Probe System respectively, the different flow patterns of local particls concentration, local particle velocity, local particle fluctuating velocity and sectionally average particle velocity in concurrent upflow and downflow gas-solid system have been investigated. It is found that the particle flow in the concurrent downflow is much more uniform radially than that in the concurrent upflow riser. The investigation of flow patterns in different flow systems is of significance to the development of a new gas-solid reactor.

Key words: particle velocity, particle concentration, flow pattern, riser, downer and LOV