H2-rich synthesis gas production over Co/Al2O 3 catalyst via glycerol steam reforming

Catalysis Communications

Volumn 12, Issue 4, 2010, Pages 292-298

  Cheng, Chin Kui ^a   Foo, Say Yei ^a   Adesina, Adesoji A ^a  

^a UNIVERSITY OF NEW SOUTH WALES   (Australia)

Author keywords

Cobalt catalyst; Glycerol steam reforming; Kinetics; Synthesis gas

Indexed keywords

ALUMINA-SUPPORTED COBALT CATALYST; BASIC SITES; CARBON DEPOSITION; CATALYST SURFACES; COBALT CATALYST; CONSUMPTION RATES; DIRECT PRODUCTION; FEED COMPOSITIONS; FIXED BED REACTOR; PHYSICOCHEMICAL PROPERTY; STEAM PARTIAL PRESSURE; STEAM REFORMING; STRONG ACIDS; SYNTHESIS GAS PRODUCTION; TEMPERATURE PROGRAMMED OXIDATION; TEMPERATURE-PROGRAMMED REDUCTION; TOTAL ORGANIC CARBON;

CARBON MONOXIDE; CHEMICAL REACTORS; CHEMISORPTION; COBALT; GLYCEROL; ORGANIC CARBON; PHYSISORPTION; STEAM; STEAM ENGINEERING; SYNTHESIS GAS; TEMPERATURE PROGRAMMED DESORPTION; X RAY DIFFRACTION; X RAY DIFFRACTION ANALYSIS;

CATALYSTS;

EID: 77958458749     PISSN: 15667367     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.catcom.2010.09.018     Document Type: Article

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