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Study on Filter Drag Due to the Change of Operation Conditions in a Pulse Air Jet-type Bag Filter[I]

충격기류식 여과집진장치에서 운전조건 변화로 인한 여과저항에 관한 연구[I]

  • Ryu, Jae-Yong (Korea Institute of Environmental Science and Technology) ;
  • Suh, Jeong-Min (Dept. of Regional environmental system engineering, Pusan National University) ;
  • Park, Jeong-Ho (Dept. of Environment engineering, Chinju National University) ;
  • Jeon, Bo-Kyung (Dept of Environment engineering, Dong-a University) ;
  • Choi, Kum-Chan (Dept of Environment engineering, Dong-a University) ;
  • Son, Yoyng-Il (Dept of Environmental Science and Technology, Tokyo Institute of Technology)
  • 류재용 (한국환경기술진흥원) ;
  • 서정민 (부산대학교 지역환경시스템) ;
  • 박정호 (진주산업대학교 환경공학과) ;
  • 전보경 (동아대학교 환경공학과) ;
  • 최금찬 (동아대학교 환경공학과) ;
  • 손영일 (동경공업대학 환경이공학창조)
  • Published : 2007.04.30

Abstract

Research results for the pressure drop variance depending on operation conditions such as change of inlet concentration, pulse interval, and face velocity, etc., in a pulse air jet-type bag filter show that while at $3kg/cm^2$ whose pulse pressure is low, it is good to make an pulse interval longer in order to form the first layer, it may not be applicable to industry because of a rapid increase in pressure. In addition, the change of inlet concentration contributes more to the increase of pressure drop than the pulse interval does. In order to reduce operation costs by minimizing filter drag of a filter bag at pulse pressure $5kg/cm^2$, the dust concentration should be minimized, and when the inlet dust loading is a lower concentration, the pulse interval in the operation should be less than 70 sec, but when inlet dust loading is a higher concentration, the pulse interval should be below 30 sec. In particular, in the case that inlet dust loading is a higher concentration, a high-pressure distribution is observed regardless of pulse pressure. This is because dust is accumulated continuously in the filter bag and makes it thicker as filtration time increases, and thus the pulse interval should be set to below 30 sec. If the equipment is operated at 1m/min of face velocity, while pressure drop is low, the bag filter becomes larger and thus, its economics are very low due to a large initial investment. Therefore, a face velocity of around 1.5 m/min is considered to be the optimal operation condition. At 1.5 m/min considered to be the most economical face velocity, if the pulse interval increases, since the amount of variation in filter drag is large, depending on the amount of inlet dust loading, the operation may be possible at a lower concentration when the pulse interval is 70 sec. However, for a higher concentration, either face velocity or pulse interval should be reduced.

Keywords

References

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