Catalytic reduction of NO by propene over LaCo1−xCuxO3 perovskites synthesized by reactive grinding
Introduction
The purification of automobile exhaust gases, especially from NO which can cause acid rain and photochemical smog, is regarded as one of the main objectives for catalytic control of air pollution. Several series of catalytic materials including supported noble metals [1], metal oxides [2], [3], mesostructured alumino-silicates [4], [5], pillared clays [6] and active carbon [7] were investigated as catalysts for NO reduction. Recently, special attention has been paid to the use of perovskite-type mixed oxides as candidates for NO elimination due to their excellent redox properties and non-stoichiometric structure. Libby early pointed out their potential application for NO reduction [8].
Up to now, some success has been met in the study of the selective catalytic reduction of NO with CO, one of the reducing gases present in the effluent of gasoline engines, using perovskite-type oxides as catalysts [9], [10], [11]. In contrast, there are much less reports on NO reduction by hydrocarbons, which are also reducing gases present in the gasoline engine exhaust.
Menezo et al. [12] pointed out that NO reduction efficiency over La0.59Sr0.39MnO3 is poor, with a maximum NO conversion to N2 of 5% at 350 °C despite an appreciable propene conversion above 95% with a flow of NO–C3H6–O2–H2O at a space velocity of 26,500 h−1. It was found that the addition of alumina as a diluent produced a cooperative effect which improved NO conversion up to 20% by simultaneously shifting the temperature of the maximum conversion from 350 °C to 400 °C. The reduction of NO by a mixture of propane and propene over YFeO3 was investigated by Lentmaier and Kemmler-Sack [13] who achieved a maximum NO reduction of 5% at 400 °C with a space velocity of 20,000 h−1 in the presence of 2% oxygen. Moreover, NO conversion can be increased up to 10% by sulfation of YFeO3 with (NH4)2SO4 solution. Furthermore, Buciuman et al. [14] described catalytic behavior of a series of Mn-based perovskites in a NO–C3H6–O2–H2O mixture at a space velocity of 14.4 cm3/(g s) with a maximum NO conversion to N2 of 20%. Thus, according to the literature, the catalytic activity of perovskite-type oxides for NO reduction by C3H6 in the presence of O2 still needs to be improved.
LaCoO3 was proposed as a good potential catalyst for the simultaneous reduction of NO and oxidation of unburnt hydrocarbon in as early as 1974 [15]. Subsequently, Co-based perovskites were applied in the hydrocarbon oxidation in our previous work [16], [17], [18]. In the present work, attempts to use Co-based perovksites as catalysts for the SCR of NO by C3H6 have been performed. Furthermore, copper containing catalysts are of special interest as they are active in a wide range of reactions for the transformation of nitrogen oxides, as reviewed by Centi and Perathoner [19]. Low coordination isolated Cu ions are regarded as the active sites for SCR of NO over Cu-zeolites [4] and our recent work showing that Cu/MCM-41 was also an active catalyst [5] indicates that the surface environment of the Cu ion is of crucial importance for the catalyst activity. Introducing Cu cations into the B sites of a perovskite structure is thus likely to yield good catalytic performances.
The major traditional drawback of perovskites is the low specific surface area (usually several m2/g) due to their preparation which involves a rather high temperature (often as high as 800 °C) to ensure the formation of the crystalline phase. This suppresses their activity and to some degree limits their application [20]. A new preparation method called reactive grinding was developed in our group for the synthesis of perovskites at room temperature via high-energy ball milling, resulting in a relatively high surface area, on the order of 100 m2/g when grinding additives are used [16], [17], [18], [21], [22].
Herein, one series of LaCo1−xCuxO3 perovskites with various atomic ratios x and possessing high specific surface areas was prepared by the reactive grinding method. The aim of this work is therefore to study the influence of Cu substitution in the B site of ABO3 solids on their physicochemical properties, emphasizing the oxygen mobility on the surface and in the lattice as well as the catalytic properties in NO reduction by propene in the presence of oxygen. It is then hoped to clarify the role of oxygen in NO reduction and propene oxidation, to determine the correlation between physicochemical properties and catalytic behavior and, finally, to propose a reaction mechanism for the catalytic reduction of NO by propene over these perovskites.
Section snippets
Preparation of perovskites
A series of LaCo1−xCuxO3 perovskites with various substitution fractions was prepared by reactive grinding. The high-energy ball milling process was applied to fully mixed powders of La2O3 (Alfa, 99.99%), Co3O4 (Baker & Adamson, 97.49%) and CuO (Aldrich, 99.98%). The La2O3 powder was first calcined at 600 °C for 24 h in order to transform any La(OH)3 to La2O3. Calculated amounts of calcined La2O3 and commercial Co3O4, CuO were mixed according to the atomic ratio of LaCo1−xCuxO3 formulas and
Catalyst physicochemical characterization
The chemical composition, BET surface area, crystallite size, pore volume and average diameter of the samples synthesized by reactive grinding after calcination at 500 °C for 5 h are listed in Table 1. The tested catalysts had acceptable specific surface areas with values of 20–30 m2/g, even after calcination at 500 °C for 5 h. Fig. 1 illustrates the X-ray diffraction patterns of LaCo1−xCuxO3 solid solutions generated by reactive grinding. The comparison of these spectra with JCPDS charts indicates
H2-TPR study
The reducibility of Co-based samples was investigated by H2-TPR to check the state of the catalyst surface and bulk, and get information needed for mechanism study. Since La3+ is non-reducible under the conditions of H2-TPR, the observed H2 consumption peaks in the TPR profile of LaCoO3 are due to the reduction of Con+ cation. As seen from Fig. 2, the H2 consumption provides evidence of the complete reduction of Co3+ to Co0 occurring in two steps, from Co3+ to Co2+ with a peak maximum at 344 °C
Conclusions
A series of Co-based perovskites was synthesized by reactive grinding with nanoscale crystal domain sizes around 10 nm and high specific surface areas of 20–30 m2/g. α-Oxygen surface concentration over lanthanum cobaltite was significantly enhanced likely due to new anion vacancies generated upon Cu substitution in lattice. This increase simultaneously accelerated the formation of nitrate species and the transformation of propene as established in TPD experiments. The better performance of
Acknowledgements
The financial support of NSERC through its industrial chair program is gratefully acknowledged. We thank Nanox Inc. for the preparation of the perovskite samples.
References (51)
- et al.
Catal. Today
(1999) - et al.
J. Catal.
(2000) Catal. Today
(1996)- et al.
J. Catal.
(2004) - et al.
Appl. Clay Sci.
(1998) - et al.
J. Colloid Interface Sci.
(2001) - et al.
Appl. Catal. B: Environ.
(2004) - et al.
Mater. Res. Bull.
(1998) - et al.
Appl. Catal. B: Environ.
(2001) - et al.
Appl. Catal. B: Environ.
(2002)