Wuxi Petrochemical Equipment CO., LTD.

China

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IPC Class
B01D 45/12 - Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces 1
B01D 50/00 - Combinations of methods or devices for separating particles from gases or vapours 1
B01J 8/00 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes 1
B04C 3/04 - Multiple arrangement thereof 1
B04C 3/06 - Construction of inlets or outlets to the vortex chamber 1
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1.

Separation device

      
Application Number 16055321
Grant Number 10758921
Status In Force
Filing Date 2018-08-06
First Publication Date 2019-10-24
Grant Date 2020-09-01
Owner
  • China University of Petroleum-Beijing (China)
  • Wuxi Petrochemical Equipment Co., Ltd. (China)
Inventor
  • Lu, Chunxi
  • Gao, Sihong
  • Fan, Yiping
  • Zhang, Dandan
  • Dai, Min
  • Zhou, Lijun

Abstract

A separation device, comprising: a third-stage cyclone housing, a separating unit, and a granule recycle and regeneration unit, wherein, the separating unit is disposed inside the third-stage cyclone housing and comprises: a cyclone separator and a moving bed coupled to each other; the granule recycle and regeneration unit comprises: a riser, a spouted bed regenerator, and a regeneration pipe connecting the spouted bed regenerator with the moving bed; the spouted bed regenerator has upper and lower ends opposing to each other, wherein, the upper end of the spouted bed regenerator is provided with a sleeve which opens downwardly, the sleeve divides an interior of the spouted bed regenerator into a fountain area and an annular gap area, and a regenerating gas outlet which is in communication with the annular gap area is provided on a side wall of the spouted bed regenerator. A centrifugal separation and intercepting filtration of the moving granular bed to fine particles can separate fine particles under low pressure drop, and can continuously separate the captured dust particles and the moving bed granules ensuring a sustainable recycling of the moving bed granules.

IPC Classes  ?

  • B01D 45/12 - Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
  • B04C 3/06 - Construction of inlets or outlets to the vortex chamber
  • B04C 3/04 - Multiple arrangement thereof
  • B04C 5/085 - Vortex chamber constructions with wear-resisting arrangements
  • B04C 5/103 - Bodies or members, e.g. bulkheads, guides, in the vortex chamber
  • B04C 5/187 - Dust collectors forming an integral part of the vortex chamber
  • C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
  • B01D 50/00 - Combinations of methods or devices for separating particles from gases or vapours
  • B01J 8/00 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes
  • C10G 11/00 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils