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Ni 기반 촉매를 이용한 HI 분해 반응 특성

Characteristics of Hydrogen Iodide Decomposition using Alumina-Supported Ni Based Catalyst

  • KIM, JI HYE (Hydrogen Laboratory, Korea Institute of Energy Research) ;
  • PARK, CHU SIK (Hydrogen Laboratory, Korea Institute of Energy Research) ;
  • KIM, CHANG HEE (Hydrogen Laboratory, Korea Institute of Energy Research) ;
  • KANG, KYOUNG SOO (Hydrogen Laboratory, Korea Institute of Energy Research) ;
  • JEONG, SEONG UK (Hydrogen Laboratory, Korea Institute of Energy Research) ;
  • CHO, WON CHUL (Hydrogen Laboratory, Korea Institute of Energy Research) ;
  • KIM, YOUNG HO (Department of Applied Chemical and Biological Engineering, Chung-nam university) ;
  • BAE, KI KWANG (Hydrogen Laboratory, Korea Institute of Energy Research)
  • 투고 : 2015.11.30
  • 심사 : 2015.12.30
  • 발행 : 2015.12.30

초록

HI decomposition reaction requires a catalyst for the efficient production of hydrogen as a key reaction for hydrogen production in sulfur-iodine thermochemical water-splitting (SI) cycle. As a catalyst used in the reaction, the performance of platinum catalyst is excellent. While, the platinum catalyst is not economical. Therefore, studies of a nickel catalyst that could replace platinum have been carried out. In this study, the characteristics of the catalytic HI decomposition on the amount of loaded nickel (Ni = 0.1, 0.5, 1, 3, 5, 10 wt%) were investigated. As the supported Ni amount increased up to 3 wt%, HI decomposition was found to increase in linear proportion. However, the conversion of $Ni/Al_2O_3$ catalyst loaded above 3 wt% was not linear. It was thought that the different HI decomposition characteristics was caused in the size and metal dispersion of Ni particles of catalyst. The physical property of catalyst before and after HI decomposition reaction was characterized by BET, chemisorption, XRD and SEM analysis.

키워드

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피인용 문헌

  1. supported Ni in the HI Decomposition of Sulfur-Iodine Process vol.67, pp.2261-236X, 2016, https://doi.org/10.1051/matecconf/20166706063