Elsevier

Journal of Catalysis

Volume 299, March 2013, Pages 222-231
Journal of Catalysis

Effects of particle size, composition, and support on catalytic activity of AuAg nanoparticles prepared in reverse block copolymer micelles as nanoreactors

https://doi.org/10.1016/j.jcat.2012.12.006Get rights and content

Abstract

Block copolymer (BCP) micelles formed by polystyrene-b-poly(4-vinylpyridine) (PS-b-P4VP) were used as nanoreactors for preparing stable bimetallic AuAg nanoparticles (NPs) with finely tunable composition and diameters. Micelles loaded with NPs were then deposited onto TiO2 and Al2O3 in order to investigate the catalytic properties of the NPs with respect to CO oxidation. The polymer matrix could be removed by thermal treatment at 400 °C under H2 or O2. Different parameters, such as support, particle size, and metal composition were varied independently, so that their influence on the catalytic activity for CO oxidation could be separated. The atomic Au/Ag ratio was varied from 1:2 to 2:1, and the highest activity was obtained for an Au/Ag ratio of 1, showing synergy effects of both metals for catalyzing CO oxidation. Using nanosized TiO2 as support and an Au/Ag ratio of 1, the nanoparticle diameter was varied between ∼3 and ∼20 nm which led to a variation of activity by a factor of ∼7 (in a continuous flow reactor at 70 °C) with the smallest particles showing the highest turnover frequencies (TOFs). In comparison, regular TiO2 as catalyst carrier showed significantly lower performance than nanostructured TiO2 while no activity was found on non-reducible γ-Al2O3. Independently, all three parameters (metal particle size, Au/Ag atomic ratio, and the support) showed significant effects on the catalytic activity.

Graphical abstract

Supported bimetallic AuAg nanoparticles, homogeneous in size and composition, can be prepared using block copolymer micelles as nanoreactors, depositing the particle-loaded micelles, and removing the polymer by thermally induced depolymerization. Independent variation of particle size, composition, and support allowed for separating effects of these parameters on the catalytic activity for CO oxidation.

  1. Download : Download high-res image (185KB)
  2. Download : Download full-size image

Highlights

► Supported AuAg nanoparticles, homogeneous in composition and size, were prepared. ► Particle size, composition, and support were controlled and varied independently. ► The PS-PVP nanoreactor shell could be completely removed from the support. ► Particles with Au/Ag = 1:1 on nanosized TiO2 show highest activity for CO oxidation. ► Both oxide support and Ag take on key roles in activating molecular oxygen.

Introduction

Extensive research work both in fundamental and in applied catalysis has been carried out in order to understand the origin of the surprising catalytic properties of gold nanoparticles (NPs) [1], [2], [3], [4], [5], [6], [7], [8], [9]. It has been well-established that the catalytic performance of supported Au NPs crucially depends on the particle size, the support, and the preparation method. For example, gold supported on so-called reducible oxides, such as TiO2, CeO2, Fe2O3, Co3O4 and MnOx [4], [10], [11], [12], [13], [14], is generally considered to be more active and stable than gold nanoparticles supported on non-reducible oxides (SiO2, Al2O3, etc.). Among the reactions studied, the catalytic oxidation of CO is probably the most intensively investigated one because gold catalyzes this reaction already at room temperature and below. This low-temperature activity opens the door to a number of industrial applications, such as gas purification in CO2 lasers, CO gas sensors, air-purification devices for respiratory protection, and – perhaps most importantly – more efficient pollution control devices for reducing industrial, environmental, and automotive emission [15], [16], [17], [18].

The reason for why the catalytic activity of Au for oxidation reactions is unexpected at first sight is its inability to dissociate O2. Suitable supports have to be chosen for sufficient activity, and intensive research was devoted to the question, how Au and the oxide support interact to provide active oxygen. Yet, another way of delivering oxygen to Au so that it can unleash its oxidation chemistry is the combination with a second metal which takes over the role of adsorbing and dissociating O2. For instance, it has been observed that bimetallic AuAg NPs show improved catalytic activity for CO oxidation, as compared to the monometallic system [19]. Recently, it was also reported that nanoporous gold, a nanostructured porous gold material, is very active for CO oxidation in spite of the fact that no oxide support is present at all and feature sizes are much larger (∼30–50 nm) [20] than those of catalytically active Au nanoparticles (<5 nm) [1], [21]. Theoretical studies revealed that Ag in an Au matrix increases the O2 adsorption energy and lowers the activation energy for dissociation [22]. Notably, silver is also a catalyst for CO oxidation, but only at much higher temperatures than gold [23], [24].

In view of these results, it seems very attractive to prepare AuAg bimetallic catalysts which are economically more viable (because of the lower Ag price) but exhibit the same favorable catalytic properties as pure Au catalysts (e.g., low-temperature activity). The question is, however, how such bimetallic catalysts can be prepared with a high degree of structural and compositional control. One of the most applied methods is deposition–precipitation (D–P) pioneered by Haruta’s group for pure Au catalysts [25]. The preparation of bimetallic particles of uniform composition and size is difficult in this way. Recently, Sandoval and coworkers achieved to prepare TiO2-supported bimetallic AuAg NPs by the D–P method [26]. However, as-prepared particles exhibited a very broad distribution of compositions which improved during catalyst activation by heating only at the cost of a broadened particle size distribution.

A very versatile approach which can overcome such problems is colloidal chemistry, providing a better control over size and structure as well as chemical composition of the particles. Since the NPs are obtained dispersed in solution, the same batch of particles can be deposited on different supports, in contrast to the D–P method. In this work, we have used block copolymer (BCP) reverse micelles as nanoreactors for synthesizing stable AuAg NPs. This method was first reported by Antonietti and coworkers [27] as well as by Möller and coworkers [28], who have well-established this technique as a method for the generation of regular arrays of monodisperse NPs on various metals and oxides. The microphase separation within the BCPs is the key to the control of particle size and interparticle distance: when BCPs are dissolved in a suitable solvent at or above their critical micelle concentration, they form reverse micelles. Adequate metal precursors added to the solution link only to the micelle cores and do not stain the shells. In a subsequent reaction step, the metal within the precursor, typically a metal salt, is reduced and aggregation of the metal into one or several particles within each micelle core is induced. Thus, the absolute diameter of the micelles and the relative dimensions of their core and shell determine the particle size. In a previous study using polystyrene-block-poly(4-vinylpyridine) (PS-b-P4VP) as a block copolymer, we could show that by choosing the proper sequence of Au and Ag addition, bimetallic AuAg nanoalloy particles can be successfully prepared with variable and controllable composition [29].

The present work pursues routes toward preparation of supported AuAg catalysts with well-defined particle size and composition by depositing, from solution, the BCP micelles loaded with AuAg NPs on various oxide supports and removing the BCP shell afterward. Being able to deposit particles from the same batch on different supports and study them under the same conditions for CO oxidation allowed us to draw clear conclusions regarding (a) the quantitative influence of particle composition, (b) the role of particle size, and (c) the role of the support.

Section snippets

Nanoparticle preparation

The colloidal synthesis of the AuAg nanoparticles inside the PS-b-P4VP block copolymer micelles is described in detail in our prior report [29]. Briefly, a PS-b-P4VP solution in toluene was loaded with AgNO3 and HAuCl4⋅H2O. Addition of hydrazine monohydrate (N2H4⋅H2O) as reducing agent then induced formation of monodisperse AuAg NPs of uniform composition, a single NP within each micelle core. The atomic ratio between Au and Ag was varied from 1:2 to 2:1 in this work. The respective

Preparation of catalysts

Fig. 1a and b show representative TEM images of PS-b-P4VP reverse micelles, loaded with AgNO3 and HAuCl4⋅H2O at an atomic Au/Ag ratio of 1:1, before and after reduction with N2H4⋅H2O, respectively. The small particulates visible in Fig. 1a are metal clusters which form throughout the PVP core due to the electron beam-induced reduction of the metal precursors in the TEM [30] and mark the dimensions of the micelle cores (10.5 ± 1.1 nm diameter, average over ∼150 micelle cores from different TEM

Conclusions

Bimetallic AuAg NPs were synthesized by using PS-b-P4VP block copolymer micelles as nanoreactors. Thereby, precise and independent control of NP size and composition was achieved. For catalytic tests, monodisperse NPs with diameters at ∼3 nm were successfully deposited onto different supports. Two different kinds of TiO2 (commercially available standard and nanostructured) and γ-Al2O3 were applied. The polymer matrix could be removed by thermal treatment in a tubular oven after optimizing

Acknowledgments

W.G.M. is grateful to the Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq – Brazil) for a fellowship. We furthermore would like to thank the University Bremen for financial support for this project.

References (55)

  • L. Jin et al.

    Ag/SiO2 catalysts prepared via γ-ray irradiation and their catalytic activities in CO oxidation

    J. Mol. Catal. A: Chem.

    (2007)
  • C.K. Costello et al.

    Nature of the active site for CO oxidation on highly active Au/gamma-Al2O3

    Appl. Catal. A – Gen.

    (2002)
  • H.H. Kung et al.

    Supported Au catalysts for low temperature CO oxidation

    J. Catal.

    (2003)
  • A.-Q. Wang et al.

    A novel efficient Au–Ag alloy catalyst system: preparation, activity, and characterization

    J. Catal.

    (2005)
  • G.C. Bond et al.

    Catalysis by gold

    Catal. Rev. – Sci. Eng.

    (1999)
  • M. Date et al.

    Vital role of moisture in the catalytic activity of supported gold nanoparticles

    Angew. Chem., Int. Ed.

    (2004)
  • S. Carrettin et al.

    Nanocrystalline CeO2 increases the activity of an for CO oxidation by two orders of magnitude

    Angew. Chem., Int. Ed.

    (2004)
  • L.M. Molina et al.

    Theoretical study of CO oxidation on Au nanoparticles supported by MgO(1 0 0)

    Phys. Rev. B

    (2004)
  • S. Arrii et al.

    Oxidation of CO on gold supported catalysts prepared by laser vaporization: direct evidence of support contribution

    J. Am. Chem. Soc.

    (2004)
  • M.S. Chen et al.

    The structure of catalytically active gold on titania

    Science

    (2004)
  • Z.P. Liu et al.

    Catalytic role of metal oxides in gold-based catalysts: a first principles study of CO oxidation on TiO2 supported Au

    Phys. Rev. Lett.

    (2003)
  • K.Y. Ho et al.

    Properties of TiO2 support and the performance of Au/TiO2 catalyst for CO oxidation reaction

    Gold Bull.

    (2007)
  • R.M.T. Sanchez et al.

    Selective oxidation of CO in hydrogen over gold supported on manganese oxides

    J. Catal.

    (1997)
  • S.D. Gardner et al.

    Catalytic behavior noble-metal reducible oxide materials for low-temperature CO oxidation. 1. Comparison of catalyst performance

    Langmuir

    (1991)
  • I. Dobrosz et al.

    Gas sensing semiconductor probes for the determination of air/fuel ratios in burning gas mixtures

    Przem. Chem.

    (2003)
  • F.G. Dwyer

    Catalysis for control of automotive emissions

    Catal. Rev.

    (1972)
  • J.H. Liu et al.

    Synergistic effect in an Au–Ag alloy nanocatalyst: CO oxidation

    J. Phys. Chem. B

    (2005)
  • Cited by (39)

    • Study on AuNPs size regulation and AuNPs/BP photocatalytic performance

      2022, Optical Materials
      Citation Excerpt :

      When the particle size of AuNPs decreased to a certain threshold, the electronic energy level of the particles can change from continuous to discrete or wider, which greatly changes the catalytic performance and optical properties of AuNPs [24]. Menezes et al. [25] deposited monodisperse Au-AgNPs with the particle size of 3 nm on TiO2 and adjusted the particle size with hydrogen at 400 °C. The results showed that the well-distributed small nanoparticles had good crystalline properties.

    • Atomic level N-coordinated Fe dual-metal embedded in graphene: An efficient double atoms catalyst for CO oxidation

      2021, Colloids and Surfaces A: Physicochemical and Engineering Aspects
      Citation Excerpt :

      Among all the strategies of reducing CO concentration in the atmosphere, the CO oxidation is one of the most effective methods for conversion of CO to CO2 and it found to have great industrial application value. For example, pollution control devices for industrial and automotive emissions [2], solving the problem of fuel cell poisoning [3], CO gas sensors, air purification equipment, etc. play an important role in control of CO emissions [4–6]. Since Haruta et al. found that gold nanoparticles supported on metal oxide can exhibit surprisingly high activity in CO oxidation at room temperature, this has attracted great attention and made supported metal nanostructures as the most widely used heterogeneous catalysts in industrial production [7].

    • Catalytic activity of gold-silver nanoalloys for HCHO oxidation: Effect of hydroxyl and particle size

      2020, Applied Surface Science
      Citation Excerpt :

      Obviously, the size of Au-Ag particles was controlled by different preparation process. This might be interpreted as that the metal mobility on the support was relevant to OH groups on the support surface [5]. The average size of AuAg alloy particles for AuAg/SBA-15(C) catalyst was 4.7 nm calculated by Scherrer's equation from XRD patterns, which was higher than the real particle size of 3.1 nm that counted in the TEM images.

    View all citing articles on Scopus
    View full text