Elsevier

Catalysis Today

Volume 175, Issue 1, 25 October 2011, Pages 603-609
Catalysis Today

Nanosized Ag/α-MnO2 catalysts highly active for the low-temperature oxidation of carbon monoxide and benzene

https://doi.org/10.1016/j.cattod.2011.04.008Get rights and content

Abstract

Nanosized α-MnO2-supported silver catalysts (xAg/nano-MnO2, x = 0–10.0 wt%) were prepared by the incipient wetness impregnation method and characterized by means of numerous analytical techniques. Catalytic activities of the materials were evaluated for the oxidation of CO and benzene. It is shown that the loading of silver on nano-MnO2 could significantly modify the catalytic activities and the catalytic performance of xAg/nano-MnO2 strongly depended upon the Ag loading, among which 5Ag/nano-MnO2 performed the best for the addressed reactions. The excellent performance of 5Ag/nano-MnO2 was associated with the highly dispersed Ag, good low-temperature reducibility, and synergism at the interface of Ag and MnO2 nanodomains.

Graphical abstract

Nanosized α-MnO2-supported silver catalysts (xAg/nano-MnO2, x = 0–10.0 wt%) are prepared by the incipient wetness impregnation method. It is shown that the catalytic performance strongly depends upon the Ag loading and 5Ag/nano-MnO2 performs the best for CO and benzene oxidation; such excellent performance is associated with the highly dispersed Ag, good low-temperature reducibility, and synergism between the Ag and MnO2 nanodomains.

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Highlights

► There is a strong interaction between Ag and nano-MnO2 nanodomains. ► Ag loading promotes the reducibility of nano-MnO2. ► Ag-loaded nano-MnO2 catalysts perform well in the oxidation of CO and benzene. ► 5Ag/nano-MnO2 shows the best catalytic activity for both reactions. ► Ag dispersion, reducibility, and synergism determine catalytic performance.

Introduction

Catalytic oxidation of carbon monoxide is of considerable interest due to its relevance in many industrial applications, such as gas purification in CO2 lasers, CO sensors, air-purification devices for respiratory protection, and pollution control devices for reducing industrial and environmental emissions [1]. Most of volatile organic compounds (VOCs) emitted from transportation and industrial activities are harmful to the atmospheric environment and human health [2], [3]. Therefore, it is of significance to eliminate the VOCs [4]. The conventional incineration of organic pollutants usually requires high temperatures (>1000 °C), resulting in a rise in energy consumption. Catalytic oxidation of VOCs, however, has been generally accepted to be one of the most effective pathways for the destruction of VOCs at lower temperatures (<500 °C). Such a catalytic strategy possesses advantages of high feasibility, low operation cost, and high destruction efficiency [5]. The catalyst employed is a key issue determining the effectiveness of catalytic oxidation technology.

In the past years, a number of materials, including supported noble metals (Pt, Pd, Rh, and Au) [6], [7], [8] and base transition-metal (Cr, Co, Cu, Ni, and Mn) oxides [6], [9], [10], have been used as catalyst for the combustion of VOCs. The former are highly active at lower temperatures, but their applications are limited due to the high cost and involved problems related to sintering, volatility, and susceptibly poisoning tendency [6], [11], [12]. Hence, there is an urgent need to develop cheaper and active catalysts that exhibit high thermal stability and great resistance to poisoning.

Bulk and/or supported manganese oxides have long been used as an active catalyst for the oxidation of carbon monoxide, methane, and hydrocarbons [13]. Since a single-component catalyst is usually hard to rival a precious metal catalyst, attempts for enhancing catalytic activity have been made by combining two or more transition-metal elements. For example, Mn–Fe composite oxides showed a higher activity than the zeolite-supported Pt material in catalyzing the oxidation of oxygen-containing organic compounds [14]. Loading a small amount of gold nanoparticles on manganese oxide (i.e., Au/MnOx) could give rise to a significant enhancement in catalytic activity for the oxidation of CO [15] and alcohol [16].

Although silver is not a good oxidation catalyst in most cases, it can be utilized as an active component of catalysts for some deep or partial oxidation. It has been demonstrated that supported silver catalysts showed good catalytic performance for the selective oxidation of ethylene to ethylene oxide [17], the oxidation of acetone and pyridine [18], and the oxidation of VOCs [19]. To the best of our knowledge, no reports on the use of nanosized MnO2-supported Ag as catalyst for benzene combustion have been seen in the literature. Recently, we have prepared numerous MnO2-supported transition-metal catalysts and found these materials performed well in the combustion of some typical VOCs. Herein, we report the preparation, characterization, and catalytic properties of nanosized Ag/MnO2 with various Ag loadings for the complete oxidation of carbon monoxide and benzene.

Section snippets

Catalyst preparation

Alpha manganese oxide was synthesized by mild reduction of aqueous solution of KMnO4 (0.12 mol/L) with maleic acid (C4H4O4, 0.040 mol/L) at a molar ratio of KMnO4/C4H4O4 = 3 at room temperature (RT). The resulting dark brown gel was kept in air at RT for 24 h, and then filtered and washed with deionized water for several times until pH = 7. After being dried at 110 °C for about 20 h, the solid was calcined in air at a ramp of 1 °C/min from RT to 450 °C and maintained at this temperature for 3 h. The

Crystal phase composition

Fig. 1 shows the XRD patterns of the as-prepared manganese oxide and its supported Ag catalysts (xAg/nano-MnO2). For the manganese oxide support, 1Ag/nano-MnO2, and 3Ag/nano-MnO2, there were diffraction peaks in the 2θ range of 20–80° (Fig. 1(a)–(c)), ascribable to the tetragonal α-MnO2 phase (JCPDS PDF# 44-0141). No significant signals assignable to Ag2O or Ag phases were detected for the 1Ag/nano-MnO2 and 3Ag/nano-MnO2 catalysts. With the rise in Ag loading from 3.0 to 5.0 wt%, however, weak

Conclusions

Nanometer α-MnO2-supported Ag catalysts (xAg/nano-MnO2) with x = 0–10.0 wt% could be prepared via the incipient wetness impregnation route. The introduction of Ag resulted in a drop in surface area of the catalyst. The Ag particles were highly dispersed on nano-MnO2 at a lower Ag loading. For the xAg/nano-MnO2 samples, the surface Mn4+/Mn3+ atomic ratios increased but the surface Oads/Olatt molar ratios decreased at elevated Ag loadings. Loading Ag could modify the reducibility of the xAg/nano-MnO2

Acknowledgements

This research was supported by National Natural Science Foundation of China (No. 20777005/B0703), Beijing Natural Science Foundation of China (No. 8082008) and Beijing Municipal Foundation for Excellent Person of Ability (No. 20071 D0501500210).

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