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Packed Bed Methane Chemical-Looping Reforming System Modeling for the Application to the Hydrogen Production

수소 생성을 위한 고정상 메탄 매체 순환 개질 시스템 모델링

  • HA, JONGJU (Graduate School of Mechanical Engineering, Yonsei University) ;
  • SONG, SOONHO (Department of Mechanical Engineering, Yonsei University)
  • 하종주 (연세대학교 대학원 기계공학과) ;
  • 송순호 (연세대학교 기계공학과)
  • Received : 2017.09.27
  • Accepted : 2017.10.30
  • Published : 2017.10.30

Abstract

A study on the modeling of the methane Chemical Looping Reforming system was carried out. It is aimed to predict the temperature and concentration behavior of the product through modeling of oxygen carrier fixed bed reactors composed of multiple stacks. In order to design the reaction system, first of all, the flow rate of the hydrogen to be produced was calculated. The flow rate ratio of the oxidation/reduction reactor was calculated considering the heat of reaction between adjacent reactors. Finally, in this paper, kinetic model including empirical coefficients was suggested.

Keywords

References

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