CIESC Journal

• RESEARCH PAPERS •    下一篇

流化床中旋风下料管的物理模型

K.Smoldersa; D.Geldartb; J.Baeyensc   

  1. a Institute for Environmental Sciences, University of Antwerp, Universiteitsplein 1, 2610
    Wilrijk, Belgium) 
    b Department of Chemical Engineering, University of Bradford, 7 Richmond Road, Bradford BD7
    1DP, United Kingdom ) 
    c Department of Chemical Engineering, Katholieke Universiteit Leuven, de Croylaan 46, 3001
    Heverlee, Belgium )
  • 收稿日期:1900-01-01 修回日期:1900-01-01 出版日期:2001-12-28 发布日期:2001-12-28
  • 通讯作者: K.Smolders

The Physical Models of Cyclone Diplegs in Fluidized Beds

K.Smoldersa; D.Geldartb; J.Baeyenscc   

  1. a Institute for Environmental Sciences, University of Antwerp, Universiteitsplein 1, 2610
    Wilrijk, Belgium) 
    b Department of Chemical Engineering, University of Bradford, 7 Richmond Road, Bradford BD7
    1DP, United Kingdom ) 
    c Department of Chemical Engineering, Katholieke Universiteit Leuven, de Croylaan 46, 3001
    Heverlee, Belgium )
  • Received:1900-01-01 Revised:1900-01-01 Online:2001-12-28 Published:2001-12-28
  • Contact: K.Smolders

摘要: In most industrial fiuidization units, two- or three-stage cyclone systems are used to
clean the product gases. To return the solids to the bed, these cyclones are fitted with
diplegs. By pass of gas from the bed through the dipleg is partially overcome by the back
pressure build-up in the dipleg and by adding a trickle valve at the bottom of the dipleg.
Diplegs of primary cyclones, operating at a high solid loading behave differently from
diplegs of secondary and tertiary cyclones which operate at low solid loading. Both types
have been investigated by pressure drop measurements, visual observation and by
measurements of the air flow rate flowing up the riser. The primary dipleg was also studied
using electrical capacitance tomography. The results are reported hereafter and will give a
first indication towards the right design of the dipleg and the selection of the trickle
valve. The influence of gas flow in the dipleg on the conversion in a catalytic fluidized
bed reactor is found to be negligible.

关键词: cyclone dipleg;fluidized bed;physical model

Abstract: In most industrial fiuidization units, two- or three-stage cyclone systems are used to
clean the product gases. To return the solids to the bed, these cyclones are fitted with
diplegs. By pass of gas from the bed through the dipleg is partially overcome by the back
pressure build-up in the dipleg and by adding a trickle valve at the bottom of the dipleg.
Diplegs of primary cyclones, operating at a high solid loading behave differently from
diplegs of secondary and tertiary cyclones which operate at low solid loading. Both types
have been investigated by pressure drop measurements, visual observation and by
measurements of the air flow rate flowing up the riser. The primary dipleg was also studied
using electrical capacitance tomography. The results are reported hereafter and will give a
first indication towards the right design of the dipleg and the selection of the trickle
valve. The influence of gas flow in the dipleg on the conversion in a catalytic fluidized
bed reactor is found to be negligible.

Key words: cyclone dipleg, fluidized bed, physical model