화학공학소재연구정보센터
검색결과 : 23건
No. Article
1 Intrinsic kinetics of steam methane reforming on a thin, nanostructured and adherent Ni coating
Minette F, Lugo-Pimentel M, Modroukas D, Davis AW, Gill R, Castaldi MJ, De Wild J
Applied Catalysis B: Environmental, 238, 184, 2018
2 Hydrogen production through the fuel processing of liquefied natural gas with silicon-based micro-reactors
Ahn SH, Choi I, Kwon OJ, Kim JJ
Chemical Engineering Journal, 247, 9, 2014
3 Genuine design of compact natural gas fuel processor for 1-kW(e) class residential proton exchange membrane fuel cell systems
Jung UH, Kim W, Koo KY, Yoon WL
Fuel Processing Technology, 121, 32, 2014
4 Methane membrane steam reforming: Heat duty assessment
De Falco M, Piemonte V, Di Paola L, Basile A
International Journal of Hydrogen Energy, 39(9), 4761, 2014
5 Investigations on the behaviour of 2 kW natural gas fuel processor
Di Bona D, Jannelli E, Minutillo M, Perna A
International Journal of Hydrogen Energy, 36(13), 7763, 2011
6 Natural gas steam reforming for hydrogen production over metal monolith catalyst with efficient heat-transfer
Roh HS, Lee DK, Koo KY, Jung UH, Yoon WL
International Journal of Hydrogen Energy, 35(4), 1613, 2010
7 Effect of calcination temperature of mesoporous nickel-alumina catalysts on their catalytic performance in hydrogen production by steam reforming of liquefied natural gas (LNG)
Seo JG, Youn MH, Chung JS, Song IK
Journal of Industrial and Engineering Chemistry, 16(5), 795, 2010
8 Hydrogen Production by Steam Reforming of Liquefied Natural Gas over Mesoporous Ni-Al2O3 Catalysts Prepared by a Co-Precipitation Method: Effect of Ni/Al Atomic Ratio
Seo JG, Youn MH, Nam I, Hwang S, Chung JS, Song IK
Catalysis Letters, 130(3-4), 410, 2009
9 Hydrogen Production by Steam Reforming of Liquefied Natural Gas Over Mesoporous Ni-Al2O3 Composite Catalyst Prepared by a Single-step Non-ionic Surfactant-templating Method
Seo JG, Youn MH, Park DR, Jung JC, Song IK
Catalysis Letters, 132(3-4), 395, 2009
10 Hydrogen production by steam reforming of liquefied natural gas (LNG) over Ni/Al(2)O(3)-ZrO(2) xerogel catalysts: Effect of calcination temperature of Al(2)O(3)-ZrO(2) xerogel supports
Seo JG, Youn MH, Park SY, Chung JS, Song IK
International Journal of Hydrogen Energy, 34(9), 3755, 2009