Stabilization of cationic gold species on Au/CeO2 catalysts under working conditions

https://doi.org/10.1016/j.apcata.2006.03.004Get rights and content

Abstract

Infrared spectroscopy of CO adsorption at low temperature has shown the presence of oxidized gold species (Au+ and Au3+) on nanocrystalline Au/CeO2 catalyst. This species are quite stable even under reduction conditions like the CO oxidation reaction. The concentration of this species decrease by increasing the pre-treatment temperature of the Au/CeO2 catalyst which is in accordance with a decrease in the catalytic activity of the sample. In accordance oxidized gold species are involved in the catalytic activity of Au/CeO2 catalyst for CO oxidation although the participation of metallic sites cannot be excluded.

Introduction

In the last years gold catalysts supported on metal oxides have been reported to be highly active for several reactions including low temperature CO oxidation [1], [2], [3]. It has been shown how the catalytic activity of these catalysts is strongly influenced by gold particle size, synthesis method, pre-treatment conditions and the nature of the support [3]. The supports have been differentiated between those able to provide oxygen (reducible) and those not able to do so because of their inability to adsorb oxygen [4]. In the case of reducible oxides supports, oxygen is thought to adsorb on the support and successively interact with the CO adsorbed on the gold particles [5], for this reason the activity is extremely dependent on the type of structure of the metal-support interface [4]. Thus, it has been presented that gold clusters supported on nanocrystalline and mesostructured nanocrystalline CeO2 or Y2O3 is much more active for oxidations [6], [7], [8] as well as for carbon–carbon bond formation [9] than gold clusters on conventional CeO2 or Y2O3 supports. More specifically, supported on nanocrystalline CeO2 presents high activity for CO oxidation [6] and the support supplies reactive oxygen (in the form of superoxide and peroxide species) to the active gold sites [10]. The interface between metallic gold particles and the support appears to be critical for high CO oxidation activity [10], [11], and time-resolved XANES spectra have shown the presence of cationic gold clusters in the Au/CeO2 catalyst, which were stable during CO oxidation [12]. The presence of Au+ and Au3+ species has also been evidenced by XPS analysis [10]. Several authors suggested the crucial role of oxidized gold species [13], [14], or even the cooperative role of metallic and oxidized gold species [15], [16] for the low temperature CO oxidation, while others propose only metallic gold as the active species [17].

In the work reported here FTIR spectroscopy has been employed, as a surface sensitive technique, in order to determine the nature of gold species present on Au/CeO2 catalysts under reaction conditions. Due to the rapid reduction at room temperature of ionic gold in contact with CO, even in the presence of oxygen, the characterisation of the catalyst was carried out by freezing down the reaction in liquid N2 and analyzing the nature of gold species using CO as a probe molecule.

Section snippets

Experimental

The catalysts were prepared starting from nanocrystalline CeO2 and HAuCl4 according to a procedure previously described [6]. As-prepared samples and H2-reduced samples at 373 and 573 K have been studied.

The catalytic tests were performed with powdered catalysts, diluted with SiC, in a 9 mm i.d. quartz reactor, at different contact times W/F=gcathmolCO1, using 2% CO–1% O2–He as gas reaction mixture (50 ml/min). The products were analyzed by gas chromatography using Porapack and Molecular Sieves

Results and discussion

The catalytic activity of gold supported on nanocrystalline CeO2 strongly depends on the catalyst pre-treatment (Fig. 1). The highest catalytic activity was obtained with the as-prepared catalyst while reduction in H2 strongly reduces the activity. Sintering of gold metal particles due to high temperature pre-treatment has been reported to decrease drastically the activity of gold supported catalysts [3]. However in this case, although the presence of metallic gold particles has been seen in

Acknowledgements

The authors thank European Union network AURICAT (HPRN-CT-2002-00174) and CICYT (MAT2003-07945-C02-01) for financial support.

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