• Title of article

    The solid flow structure in a circulating fluidized bed riser/downer of 0.42-m diameter

  • Author/Authors

    Zhang، نويسنده , , Minghui and Qian، نويسنده , , Zhen and Yu، نويسنده , , Hao and Wei، نويسنده , , Fei، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2003
  • Pages
    7
  • From page
    46
  • To page
    52
  • Abstract
    Local transient solid fraction and particle velocity signals were measured in a 0.418-m I.D. and 18-m high large-scale circulating fluidized bed (CFB) by a dual-optical fiber density probe and a Laser Doppler Velocimeter (LDV) system. The probability density distributions (PDD) of transient solid fraction and particle velocity show bimodal distributions in the riser, while in the downer, the PDD curves only exhibit single peak distribution. The results indicate that two-phase solid flow structure exists in the riser: i.e. a dense cluster phase and a dispersed particle phase. Although there are solid aggregations in the downer, the solid concentration of which is much lower than that in the riser, and they could not form a dense cluster phase with solid fraction 1−εmf as those in the riser. From the analysis and comparison of transient solid fraction signal and the PDD of solid fraction and particle velocity in the riser and downer, it is clear that significant difference exist in the solid flow structure and the particle cluster mechanism between the gravity-assisted gas–solid flow in the downer and the against-gravity flow in the riser.
  • Keywords
    Solid flow structure , Riser , Large-scale , Probability density distribution (PDD) , Downer
  • Journal title
    Powder Technology
  • Serial Year
    2003
  • Journal title
    Powder Technology
  • Record number

    1692113