Synthesis gas production to desired hydrogen to carbon monoxide ratios by tri-reforming of methane using Ni-MgO-(Ce,Zr)O2 catalysts

Applied Catalysis A: General

Volumn 445-446, Issue , 2012, Pages 61-68

  Walker, Devin M ^a   Pettit, Sandra L ^a   Wolan, John T ^a   Kuhn, John N ^a  

^a UNIVERSITY OF SOUTH FLORIDA   (United States)

Author keywords

Biofuel; Energy; Fischer Tropsch synthesis; Gas to liquid; Hydrogen production

Indexed keywords

CATALYST CHARACTERIZATION; CATALYST LIFETIME; CATALYST PERFORMANCE; COKE FORMATION; CONTROLLED REACTION CONDITIONS; DEPOSITION PRECIPITATION METHODS; ENERGY; FEED GAS COMPOSITION; FT SYNTHESIS; GAS-TO-LIQUID; HIGH CONVERSIONS; METAL LOADINGS; REACTANT CONVERSION; REACTION CONDITIONS; REACTION PERFORMANCE; SEM-EDS; SYNTHESIS GAS PRODUCTION; SYNTHESIS PARAMETERS; WET IMPREGNATION; WET IMPREGNATION METHOD; XRD;

BIOFUELS; CARBON DIOXIDE; CARBON MONOXIDE; CATALYST DEACTIVATION; FISCHER-TROPSCH SYNTHESIS; HYDROGEN PRODUCTION; IMPREGNATION; LOADING; METHANE; PRECIPITATION (CHEMICAL); STEAM REFORMING; SYNTHESIS (CHEMICAL); SYNTHESIS GAS; ZIRCONIUM;

CERIUM;

EID: 84870328341     PISSN: 0926860X     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.apcata.2012.08.015     Document Type: Article

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