• Title/Summary/Keyword: Reforemer

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A Study of Partial Oxidation of Methane by Pd Catalyst - Effects of Reaction Temperature - (팔라듐 촉매의 메탄 부분산화에 관한 연구 - 반응온도에 따른 효과 -)

  • Lee, Taek-Hong;Mun, Yeong-Hwan
    • Transactions of the Korean hydrogen and new energy society
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    • v.15 no.3
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    • pp.244-249
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    • 2004
  • Pd catalyst have been used in hydrogenation, oxidation, and low temperature combustion reaction. Recently, it has been candidated as a possible reagents in the partial oxidation of methanol reformers of the fuel cell. Pd catalysts, even though it is very precious and expensive, catalytic functioning is good, but it still need to be improved in the matter of durability and low catalytic activity after calcination. In this study, we synthesize the improved Pd catalyst and study their chemical functioning.

Propane Reforming in Gliding Arc Plasma Reformer for SynGas Generation (합성가스 생성을 위한 글라이딩 아크 플라즈마 개질기에서 프로판 개질)

  • Yang, Yoon-Cheol;Chun, Young-Nam
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.33 no.11
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    • pp.869-875
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    • 2009
  • The purpose of this paper is to investigate the optimal condition of the syngas production by reforming of propane using Gliding arc plasma reformer. The gliding arc plasma reformer in 3 phases has been newly designed and developed with a quick starting and fast response time. It can be applicable to the various types of fuels (Hydrocarbons $C_xH_y$), and it has a high conversion rate of fuels and high production of hydrogen. The parametric screening studies were carried out according to the changes of a steam feed amount i.e., steam/carbon ratio, total gas flow rate and input electric power. The optimum operating conditions were S/C ratio 2.8, total gas flow rate of 14 L/min and input electric power of 2.4 kW. The result of optimum operating conditions showed the 55 % $H_2$, 14 % CO, 15 % $CO_2$, 10 % $C_3H_8$ and 4 % $CH_4$. Also, $C_3H_8$ conversion, $H_2$ yield and $H_2$ selectivity were 90 %, 42 %, 15 %, respectively. The energy efficiency and specific energy requirements were 37 % and 334 kJ/mol respectively.