Synthesis, structure and three way catalytic activity of Ce1−xPtx/2Rhx/2O2−δ (x = 0.01 and 0.02) nano-crystallites: Synergistic effect in bimetal ionic catalysts
Graphical abstract
Bimetal ionic Ce1−xPtx/2Rhx/2O2−δ (x = 0.01 and 0.02) catalyst with Pt in 2+ and Rh in 3+ states is synthesized by a single step solution combustion method. The bimetal ionic catalyst induces reduction of Rh3+ at a lower temperature in presence of Pt2+ ion compared to the corresponding mono-metal ionic catalysts, Ce1−xPtxO2−δ and Ce1−xRhxO2−δ, showing enhanced catalytic activity as well as synergistic effect.
Introduction
Bimetallic catalysts often exhibit improved properties than either of the single metal catalysts. This is called synergistic effect. The presence of the synergistic activity of platinum and rhodium in bimetallic catalysts and possible reasons for the effects has been discussed in literatures [1], [2], [3], [4], [5], [6], [7]. The synergistic effects in Pt–Rh bimetallic catalysts have been shown over alumina-supported catalysts for CO oxidation and NO + CO reactions [8], [9], [10], [11], [12], [13], [14]. The presence of synergism in Pt–Rh/Al2O3 system is generally explained as due to Pt–Rh alloying effect. The decay in the activity of rhodium catalysts at high temperature is explained as due to: (a) formation of reduction resistive oxide layer on the alumina surface or (b) formation of rhodium aluminate. When Pt is present together with Rh, reduction of Rh is promoted, thereby leading to synergistic alloying effect.
Factors which contribute to the catalytic properties of a bimetallic catalyst include: (a) the surface composition of the noble metal and (b) the strength of interaction between the noble metal and the catalyst support. For alumina-supported platinum catalysts, Chu et al. [15] suggested the sintering of the dispersed particles as an important factor in catalyst deactivation, indicating weak interaction between platinum and alumina. Too strong metal–support interaction may also lead to decreased catalytic activity, as suggested for alumina-supported rhodium [16], [17], [18]. Mechanism of this deactivation is still unclear [19], [20], [21]. When both Pt and Rh are added to the support, the synergistic effect of platinum and rhodium is shown to be capable of stabilizing rhodium against the formation of a reduction-resistive oxide phase on alumina support as shown by Polvinen et al. for bimetallic Pt–Rh catalysts with pure alumina and CeZrO2-modified alumina washcoat [22].
There are a few studies on bimetallic Pt–Rh/CeO2 catalysts [22], [23], [24], [25], [26], [27]. The effects of high temperature redox ageing on this catalytic system have been studied. The nature of the active sites of the catalyst in this bimetallic system is debated.
In recent years, we have studied the single metal Pt and Rh ion substitution in ceria as in Ce1−xPtxO2−δ and Ce1−xRhxO2−δ (x = 0.01 and 0.02) catalysts, where Pt2+, Rh3+ ions are shown to be the active sites for adsorption [28], [29], [30]. These oxide solid solutions can be called mono-metal ionic catalysts. What can be the combined effect when both Pt and Rh are present as ions in the ceria supported catalyst? To understand this we have studied the structure, redox properties, CO and C2H4 oxidation, and NO reduction activity of Ce1−xPtx/2Rhx/2O2−δ (x = 0.01 and 0.02) bimetal ionic catalysts and compared them with their corresponding mono-metal ionic analogue, namely, Ce1−xPtxO2−δ and Ce1−xRhxO2−δ.
Section snippets
Experimental
The catalysts have been synthesized by the combustion of aqueous stoichiometric composition of (Pt, Rh) metal chloride, ceric ammonium nitrate with oxalyl dihydrazide (C2H6N4O2, ODH) as the fuel. Specifically, for the preparation of Ce0.99Pt0.005Rh0.005O2−δ, (NH4)2Ce(NO3)6, H2PtCl6, RhCl3·xH2O and ODH were taken in the mole ratio 0.99:0.005:0.005:2.376. A typical preparation consisted of dissolving 10 g of (NH4)2Ce(NO3)6 (E. Merck India Ltd., 99.9%), 4.77 ml of 1% H2PtCl6 (1 g H2PtCl6 dissolved in
XRD studies
Diffraction lines of the catalysts could be indexed to the fluorite structure of ceria. The sizes of the (Pt2+ and Rh3+ ion substituted) CeO2 crystallites were obtained from the Scherrer formula. Crystallite sizes are in the range 40–50 nm (see Table 1). The XRD patterns of PtRhC1, PtRhC1(HT), PtRhC2 and PtRhC2(HT) catalysts, in the 2θ range 25–50° are magnified by 30 times in the Y scale with respect to CeO2(1 1 1) peak and they are given in Fig. 1(a–d). XRD patterns of RhC1(HT) and PtC1(HT) are
Conclusions
In this study, activity of bimetal ionic catalyst is compared with the corresponding mono-metal ionic catalysts and the important conclusions are:
- (i)
A single step solution combustion method can be employed to synthesize Ce1−xPtx/2Rhx/2O2−δ (x = 0.01 and 0.002).
- (ii)
Hydrogen uptake study shows a lower temperature reduction of Rh3+ ion in the bimetal ionic catalysts compared to mono-metal ionic Ce1−xRhxO2−δ catalyst.
- (iii)
Synergistic effect of bimetal Pt2+, Rh3+ ion catalyst, Ce1−xPtx/2Rhx/2O2−δ, is shown to be
Acknowledgements
A. Gayen is thankful to Council of Scientific and Industrial Research (CSIR), Government of India for the award of a research fellowship. Thanks are due to C.R. Reddy, B.V. Kumar and N. Mahadeva, Bangalore Institute of Technology (BIT), for surface area measurement. Financial assistance from the Department of Science and Technology (DST), Government of India is gratefully acknowledged.
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Present address: Department of Chemistry, Physical Chemistry Section, Jadavpur University, Kolkata 700032, India.