An Experimental Study on the Heat and Mass Transfer of Adsorption Chiller

흡착식 냉동기의 열 및 물질전달에 관한 실험적 연구

  • Kwon Oh-Kyung (Applied Energy System Team, Korea Institute of Industrial Technology) ;
  • Yun Jae-Ho (Applied Energy System Team, Korea Institute of Industrial Technology) ;
  • Joo Young-Ju (Graduate School of Mechanical Engineering, Korea University) ;
  • Kim Yong-Chan (Department of Mechanical Engineering, Korea University) ;
  • Kim Joung-Ha (Applied Energy System Team, Korea Institute of Industrial Technology)
  • 권오경 (한국생산기술연구원 에너지응용팀) ;
  • 윤재호 (한국생산기술연구원 에너지응용팀) ;
  • 주영주 (고려대학교 대학원 기계공학과) ;
  • 김용찬 (고려대학교 기계공학과) ;
  • 김종하 (한국생산기술연구원 에너지응용팀)
  • Published : 2005.08.01

Abstract

Adsorption chillers have been receiving considerable attentions as they are energy-saving and environmentally benign systems. In order to evaluate adsorption rates, experiments were performed in the batch type adsorption apparatus. Three types of silica gels were investigated under an assortment of experimental conditions that are representatives of the actual operating environments in the adsorber of adsorption chillers. Experimental results revealed the effects of silica gel particle size, bed temperature, and fin pitch of fin tube on the adsorption rate. The $0.25\~1.18mm$ particle size of silica gel with high adsorption rate was selected as a suitable adsorbent. The measured adsorption rate became bigger with decreasing particle size. From the comparison of adsorption rate, it is found that the fin tube has about $21\%$ higher value than that of the bare tube. The effect of heat and mass flux is found to be more significant in the fin tube than in the bare tube.

Keywords

References

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