Hydrogen production by steam reforming of liquefied natural gas (LNG) over mesoporous nickel-alumina composite catalyst prepared by an anionic surfactant-templating method

Catalysis Today

Volumn 146, Issue 1-2, 2009, Pages 44-49

  Seo, Jeong Gil ^a   Youn, Min Hye ^a   Park, Sunyoung ^a   Park, Dong Ryul ^a   Jung, Ji Chul ^a   Chung, Jin Suk ^b   Song, In Kyu ^a  

^a Seoul National University   (South Korea)

^b University of Ulsan   (South Korea)

Author keywords

Anionic surfactant; Hydrogen production; Liquefied natural gas; Nickel alumina catalyst; Steam reforming

Indexed keywords

CARBON DEPOSITION; CARBON SPECIES; CATALYTIC PERFORMANCE; DEHYDROGENATION REACTIONS; GASIFICATION REACTION; HIGH SURFACE AREA; HYDROCARBON SPECIES; IMPREGNATION METHODS; INITIAL STAGES; MESO-PORES; MESOPOROUS; MESOPOROUS ALUMINA; NICKEL ALUMINATE; NICKEL CATALYST; NICKEL SURFACES; NICKEL-ALUMINA; NICKEL-ALUMINA CATALYST; PORE BLOCKING; REDUCTION PROCESS; STEAM REFORMING; TEMPLATING METHOD;

ALUMINUM; ANIONIC SURFACTANTS; BIOPHYSICS; CATALYSIS; CATALYST ACTIVITY; CATALYST DEACTIVATION; CATALYST POISONING; DEHYDROGENATION; DISPERSIONS; GAS FUEL PURIFICATION; GAS INDUSTRY; GAS PRODUCERS; HYDROCARBONS; HYDROGEN PRODUCTION; LIQUEFIED NATURAL GAS; NICKEL ALLOYS; SINTERING; STEAM; STEAM ENGINEERING; STRUCTURE (COMPOSITION);

NICKEL;

EID: 67849087065     PISSN: 09205861     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cattod.2008.12.008     Document Type: Article

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