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Characteristics of Ni/3d Series Transition Metal/γ-Al2O3 Catalysts and their Hydrogen Production Abilities from Butane Steam Reforming
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  • Characteristics of Ni/3d Series Transition Metal/γ-Al2O3 Catalysts and their Hydrogen Production Abilities from Butane Steam Reforming
  • Characteristics of Ni/3d Series Transition Metal/γ-Al2O3 Catalysts and their Hydrogen Production Abilities from Butane Steam Reforming
저자명
Lee. Jun-Su,Choi. Byung-Hyun,Ji. Mi-Jung,Kang. Mi-Sook
간행물명
Bulletin of the Korean Chemical Society
권/호정보
2011년|32권 9호|pp.3281-3289 (9 pages)
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대한화학회
파일정보
정기간행물|ENG|
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이 논문은 한국과학기술정보연구원과 논문 연계를 통해 무료로 제공되는 원문입니다.
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기타언어초록

The materials composed of the 3d series transition metals are introduced into the hydrocarbon steam-reforming reaction in order to enhance the $H_2$ production and abruptly depress the catalytic deactivation resulting from the strong sintering between the Ni component and the ${gamma}-Al_2O_3$ support. The conventional impregnation method is used to synthesize the Ni/3d series metal/${gamma}-Al_2O_3$ materials through the sequentially loading Ni source and the 3d series metal (Ti, V, Cr, Mn, Fe, Co, Cu, and Zn) sources onto the ${gamma}-Al_2O_3$ support. The Mnloaded material exhibits a significantly higher reforming reactivity than the conventional Ni/${gamma}-Al_2O_3$ and the other Ni/3d series metal/${gamma}-Al_2O_3$ materials. Particularly the addition of Mn selectively improves the $H_2$ product selectivity by eliminating the formation of $CH_4$ and CO. The $H_2$ production is maximized at a value of 95% over Ni(0.3)/Mn(0.3)/${gamma}-Al_2O_4$(1.0) with a butane conversion of 100% above $750^{circ}C$ for up to 55 h.