효율적 수소 생산을 위한 메탄 수증기 개질 반응기에서의 불연속적 가스 유입의 영향

Effect of discontinuous mixture gas feeding on effective hydrogen production in a steam reformer frommethane

  • 이신구 (KAIST 기계공학과 신에너지변환시스템연구실) ;
  • 박준근 (KAIST 기계공학과 신에너지변환시스템연구실) ;
  • 임성광 (KAIST 기계공학과 신에너지변환시스템연구실) ;
  • 배중면 (KAIST 기계공학과)
  • 발행 : 2008.10.16

초록

Steam reforming reaction is a matured technology to get hydrogen from hydrocarbon fuels compared with other reforming reactions such as partial oxidation(POX), autothermal reforming(ATR). It is so endothermic that it needs heat source to activate the reaction. Due to the reaction characteristics, heat transfer limitation phenomena generally occur in the steam reformer. As one of new ideas, the effect of discontinuous gas feeding is investigated based on heat transfer characteristics. The new operating method is usually favorable at high GHSV region(i.e. over $10,000h^{-1}$). In order to numerically simulate the physical issues, numerical approach is adopted based on heterogeneous reaction model, two-equation model in energy equation, and other constitutive models in porous media.

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