Counting Au catalytic sites for the water-gas shift reaction

Abstract

We have developed various techniques to count catalytic sites of Au/TiO2 catalysts for the water-gas shift (WGS) reaction. Addition of Br in an amount that is only 16% of the moles of the surface Au on a 2.3 wt.%Au/TiO2 catalyst decreases the majority of its WGS reaction rate per total mole of Au but does not result in an appreciable change in the average Au particle size. Au particle shape, apparent activation energy, or reaction orders. From transient isotopic switch experiments, the WGS turnover frequency (TOF) for Au/TiO2 catalysts with and without Br, based on the operating active sites counted in the experiment, is 1.6 +/- 0.5 s(-1) under 6.8% CO, 8.5% CO2, 11.0% H2O. 37.4% H-2 at 120 degrees C. The estimated number of potential active sites, similar to 2% of the total amount of Au on the 2.3 wt.%Au/TiO2 catalyst, best correlates with the Au corner atoms (similar to 2%) of the cubo-octrahedral particles. From operando FTIR spectroscopy, the normalized IR peak area of CO adsorbed on Au-0 near 2100 cm(-1) is proportional to the WGS reaction rate for Au/TiO2 catalysts with and without Br. Thus, the dominant active sites on Au/TiO2 catalysts for the WGS reaction are taken to be the metallic corner Au sites with Au-Au coordination number of 4. (C) 2012 Elsevier Inc. All rights reserved.

Keywords

Water-gas shift; Gold; Bromine poisoning; WGS kinetics; Transient isotopic switch; Operando FTIR; ISOTOPIC TRANSIENT ANALYSIS; CO OXIDATION; GOLD CLUSTERS; AU/TIO2 CATALYSTS; ACTIVE-SITE; NANOPARTICLES; SIZE; HYDROGEN; TITANIA; ALUMINA

DOI

10.1016/j.jcat.2012.06.008

Citation

Journal of Catalysis Volume 293, September 2012, Pages 94–102

Date of this Version

9-2012

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