Kinetics and Mechanism of the Low-Temperature Water-Gas-Shift Reaction on Au/CeO2 Catalysts

Canadian Institute of Mining, Metallurgy and Petroleum
M. Kinne
Organization:
Canadian Institute of Mining, Metallurgy and Petroleum
Pages:
16
File Size:
387 KB
Publication Date:
Oct 1, 2003

Abstract

Catalyst preparation/ characterization Slightly modified DP (~Schumacher et al. Catal. Lett. 89, 109, 2003) CeO2 HAS 15 from Rhodia calcined in air for~ 2h BET: ~188m2/g, particles size: 5.7nm (TEM, XRD) + HAuCl4 at pH of 6.5-7, (>95% of the Au was deposited) ? Au/CeO2 (2.6wt% Au, ICP-AES) A new conditioning procedure was applied, including heating at low temperature in N2 and H2/N2 mixtures) Patent DE 10205873A1. Very small Au particles <2nm, for CO oxidation catalyst as Au/TiO2, Au/Fe2O3, and Au/Co2O3 Here Au particles size <3.5nm (XRD) Summary ? CO is nearly exclusively adsorbed on the Au particles ? Positive reaction orders of 0.5 are found for CO and H2O ? Ea= 40kJ/mol ? The catalyst is very active and stable ? During WGS reaction huge amounts of formates are formed and cover the surface ? The activity of the catalyst seems to be correlated with the formate species.
Citation

APA: M. Kinne  (2003)  Kinetics and Mechanism of the Low-Temperature Water-Gas-Shift Reaction on Au/CeO2 Catalysts

MLA: M. Kinne Kinetics and Mechanism of the Low-Temperature Water-Gas-Shift Reaction on Au/CeO2 Catalysts. Canadian Institute of Mining, Metallurgy and Petroleum, 2003.

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