Hydrodynamic Characteristics of Circulating Fluidized Bed in Different Mass Inventories

순환유동층에서 Solid Mass Inventory에 따른 수력학적 특성 연구

  • 김은경 (연세대학교 기계공학과) ;
  • 신동훈 (연세대학교 CT(Clean Tech.) 연구단) ;
  • 황정호 (연세대학교 기계공학과) ;
  • 이종민 (한국전력연구원 발전연구실) ;
  • 김재성 (한국전력연구원 발전연구실)
  • Published : 2002.11.15

Abstract

This paper discusses hydrodynamic characteristics of cold circulating fluidized bed(CFB) in different solid mass inventories. Operating parameters of solid mass inventory, primary air and J-valve fluidizing air were varied to find out the effect on the flow fludization pattern. Experimental measurements were made in a 3m tall CFB that has 0.05m riser diameter and black silica-carbonate of particle sizes from $100{\mu}m$ to $500{\mu}m$ were employed as the bed material. The operating conditions of superficial gas velocity and J-valve fluidizing velocity were in the ranges of 1.39~3.24 m/s and 0.139~0.232 m/s respectively. The axial solid fraction and solid circulation rate of CFB were observed and compared with modelling through IEA-CFBC Model and commercial CFD code.

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