Abstract
We have developed various techniques to count catalytic sites of Au/TiO 2 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/TiO 2 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/TiO 2 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% CO 2, 11.0% H 2O, 37.4% H 2 at 120 °C. The estimated number of potential active sites, ∼2% of the total amount of Au on the 2.3 wt.%Au/TiO 2 catalyst, best correlates with the Au corner atoms (∼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/TiO 2 catalysts with and without Br. Thus, the dominant active sites on Au/TiO 2 catalysts for the WGS reaction are taken to be the metallic corner Au sites with Au-Au coordination number of 4.
| Original language | English |
|---|---|
| Pages (from-to) | 94-102 |
| Number of pages | 9 |
| Journal | Journal of Catalysis |
| Volume | 293 |
| DOIs | |
| State | Published - Sep 2012 |
Keywords
- Bromine poisoning
- Gold
- Operando FTIR
- Transient isotopic switch
- Water-gas shift
- WGS kinetics
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