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Catalytic behavior of transition metal oxide in graphite gasification by oxygen, water, and carbon dioxide

Journal Article · · Journal of Catalysis; (United States)
;  [1]
  1. State Univ. of New York, Buffalo (USA)
Vanadium oxide is used as a model transition metal-oxide catalyst for the gasification of graphite by O{sub 2}, H{sub 2}O, and CO{sub 2}. The following catalyst actions on the graphite basal plane are common in all three reactions: deep layer channeling, monolayer channeling, edge recession, and widening monolayer channeling. The steady-state oxidation states of vanadium in the reactions with CO{sub 2} and H{sub 2}O are, respectively, V{sub 3}O{sub 5} and V{sub 2}O{sub 3} under the reaction conditions. The rate-limiting step in all channeling actions (for all three gasification reactions) is oxidation on the surface of the metal-oxide to increase the oxygen activity. Oxygen then diffuses through the nonstoichiometric metal-oxide particle to reach the carbon active sites where gasification takes place. (However, based on the channeling and TGA rate data, the catalyst surface oxidation is the rate-limiting step; the subsequent steps of diffusion of oxygen anion and C-C bond breakage steps are not rate-limiting.) This mechanism can explain the fact that transition metal-oxides are the most active catalysts for the C + O{sub 2} reaction but are only weakly active for the C + H{sub 2}O and C + CO{sub 2} reactions. The origin of the phenomenon of the widening monolayer channels is attributed to the anisotropy of the catalyzed reactivities of two adjacent zigzag edges of graphite.
OSTI ID:
5455393
Journal Information:
Journal of Catalysis; (United States), Journal Name: Journal of Catalysis; (United States) Vol. 130:1; ISSN 0021-9517; ISSN JCTLA
Country of Publication:
United States
Language:
English