Iowa State University From the SelectedWorks of Wenyu Huang 2011 Rh1−xPdxnanoparticle composition dependence in CO oxidation by oxygen: catalytic activity enhancement in bimetallic systems James Russell Renzas, University of California - Berkeley Wenyu Huang, University of California - Berkeley Yawen Zhang Michael E. Grass Dat Tien Hoang, University of California - Berkeley, et al. Available at: http://works.bepress.com/wenyu_huang/9/ View Article Online / Journal Homepage / Table of Contents for this issue PCCP Dynamic Article Links Cite this: Phys. Chem. Chem. Phys., 2011, 13, 2556–2562 PAPER Published on 24 December 2010. Downloaded by Iowa State University on 07/12/2015 20:26:49. www.rsc.org/pccp Rh1 xPdx nanoparticle composition dependence in CO oxidation by oxygen: catalytic activity enhancement in bimetallic systems James Russell Renzas,ab Wenyu Huang,ab Yawen Zhang,bc Michael E. Grass,de Dat Tien Hoang,a Selim Alayoglu,a Derek R. Butcher,af Franklin (Feng) Tao,waf Zhi Liud and Gabor A. Somorjai*af Received 18th September 2010, Accepted 2nd December 2010 DOI: 10.1039/c0cp01858a Bimetallic 15 nm Rh1 xPdx nanoparticle catalysts of five different compositions and supported on Si wafers have been synthesized, characterized using TEM, SEM, and XPS, and studied in CO oxidation by O2 in two pressure regimes: atmospheric pressure and 100–200 mTorr. The RhPd bimetallic nanocrystals exhibited similar synergetic effect of increased reaction activity at both atmospheric (760 Torr) and moderate (100–200 mTorr) pressures compared with pure Pd or Rh. The magnitude of the effect depends on the relative pressures of the CO and O2 reactant gases and the reaction temperature. The catalytic activity of the nanocrystals measured at moderate pressure is directly correlated to the APXPS studies, which were carried out in the same pressure. The APXPS studies suggest that the Pd–Rh interfaces are important for the enhanced activity of the bimetallic nanoparticles. Introduction Bimetallic catalysts are frequently utilized for industrial applications and they are important model systems for furthering the understanding of catalytic mechanisms and processes. These catalysts often exhibit increased activity, favorable selectivity, and reduced rates of deactivation.1–9 For example, one recent study by Stamenkovic et al. on a Pt3Ni(111) single crystal in the oxygen reduction reaction demonstrated a 10-fold enhancement in catalytic activity over the corresponding Pt(111) surface.1 This effect was determined to be a result of compositional oscillation in the top three layers of the catalysts. Another study by Gao et al. found that CO oxidation kinetics on AuPd(100) depend on whether Pd sites are isolated or contiguous, because of significant differences in CO binding on the two types of sites.2 a Department of Chemistry, University of California, Berkeley, CA 94720, USA b Chemical Sciences Division, Lawrence Berkeley National Laboratory, Berkeley, CA 94720, USA c College of Chemistry and Molecular Engineering, and the State Key Lab of Rare Earth Materials Chemistry and Applications & PKU-HKU Joint Lab in Rare Earth Materials and Bioinorganic Chemistry, Peking University, Beijing 100871, China d Advanced Light Source, Lawrence Berkeley National Laboratory, Berkeley, CA 94720, USA e Department of Applied Physics, Hanyang University, Ansan, Korea 426-791 f Materials Science Division, Lawrence Berkeley National Laboratory, Berkeley, CA 94720, USA. E-mail: [email protected] w Current address: Department of Chemistry and Biochemistry, University of Notre Dame, Notre Dame, IN 46556, USA. 2556 Phys. Chem. Chem. Phys., 2011, 13, 2556–2562 The studies by Stamenkovic and Gao both used bimetallic single crystals. Single crystals, however, are known to behave quite differently from nanoparticles.10 Nanoparticle reactivity is often dependent on size and oxidation state,11 in part because small particles can oxidize much more easily than large particles and, especially, single crystals. In order to expand control and understanding of bimetallic nanoparticle catalysts there is a need for detailed studies on the roles of nanoparticle size, surface composition, and in situ oxidation state on catalytic behavior. Among the large number of possible nanoparticle compositions, Rh, Pt, and Pd-based mono-, bi-, and trimetallic nanocrystals with controlled composition, size, and shape are of special interest because of their role in three-way automotive exhaust catalysis.12 Although CO oxidation has been studied extensively, many open questions remain regarding catalyst behavior in these systems, especially with regard to composition and oxidation state13,14 and how these factors affect catalyst deactivation,15 synergism,16 and surface segregation.17 Previous work in our lab on 15 nm Rh0.5Pd0.5 bimetallic Pd-core Rh-shell nanoparticles supported on Si wafers used ambient pressure X-ray photoelectron spectroscopy (APXPS) to examine the dependence of surface composition and oxidation state on the local chemical environment.17 This study found significant reversible changes in the catalyst composition when the nanoparticles were exposed to NO, CO, O2, H2, and mixtures of NO + CO at 300 1C. However, the catalytic reaction kinetics and surface composition of these nanoparticles has not previously been studied under the CO oxidation reaction conditions. This journal is c the Owner Societies 2011 Published on 24 December 2010. Downloaded by Iowa State University on 07/12/2015 20:26:49. View Article Online In this work, the synthesis of near-monodisperse Rh1 xPdx (x = 0–1) nanocrystals at a constant size of 15 nm by a one-step polyol method is reported. The as-synthesized bimetallic nanocrystals have Rh-rich surfaces. The RhPd bimetallic nanoparticle catalysts showed activity enhancement (synergy) in CO oxidation by O2 compared with pure Pd or Rh. APXPS studies showed that CO interacts more strongly with Pd than with Rh, while O2 has the opposite behavior. Based on the observation from APXPS studies, the reaction synergy could be explained by spillover of O atoms from Rh onto CO- and/or C-covered Pd reaction sites under reaction conditions. Experimental details (1) Nanoparticle synthesis Rhodium(III) acetylacetonate (Rh(acac)3, 97%), palladium(II) acetylacetonate (Pd(acac)2, 99%), 1,4-butanediol (99%), and poly(vinylpyrrolidone) (PVP, Mw = 55 000) were purchased from Sigma-Aldrich. All the solvents, including acetone, ethanol, hexane, and chloroform, were of analytical grade and were used without further purification. Given amounts of Rh(acac)3 and Pd(acac)2 (0.1 mmol total) and 1 mmol PVP (monomer concentration) were added to 20 ml of 1,4-butanediol in a 50 ml three-necked flask at room temperature (Table 1). The stock solution was heated to 50 1C using a Glas-Col electromantle (60 W, 50 ml) with a Cole-Parmer temperature controller (Diqi-senses), and was evacuated at this temperature for 20 min to remove water and oxygen under magnetic stirring, resulting in an optically transparent orange-yellow solution. The flask was then heated to 220 1C at a rate of 10 1C min 1 and maintained at this temperature (2 1C) for 1.5 h under Ar. During the reaction the color of the solution gradually turned from orange-yellow to black. When the reaction was complete an excess of acetone was poured into the solution at room temperature to form a cloudy black suspension. This suspension was separated by centrifugation at 4200 rpm for 6 min and the black product was collected by discarding the colorless supernatant. The precipitated Rh1 xPdx nanocrystals were washed with acetone once then re-dispersed in ethanol. The synthetic procedure used to produce Pd nanocrystals was the same as that used to synthesize Rh1 xPdx (x = 0.2–0.8) nanocrystals, except that 0.1 mmol Pd(acac)2 was added to Table 1 Synthetic conditions, lattice constants, and crystallite sizes of PVP-capped Rh1 xPdx (x = 0–1) nanocrystals Sample Rh(acac)3/ Pd(acac)2/ mmol mmol T/1C t/h a/nm Size/nm Rh Rh0.8Pd0.2 Rh0.6Pd0.4 Rh0.5Pd0.5 Rh0.4Pd0.6 Rh0.2Pd0.8 Pd 0.2 0.08 0.06 0.05 0.04 0.02 0 0.385 0.385 0.387 0.387 0.390 0.397 0.395 14.4 15.1 15.4 16.0 15.1 14.9 15.6 a 0 0.02 0.04 0.05 0.06 0.08 0.1 205 220 220 220 220 220 220 2 1.5 1.5 1.5 1.5 1.5 0.5 The standard deviation statistic from 100 nanocrystals. This journal is c the Owner Societies 2011 1.4a 2.9 2.4 1.9 2.0 2.0 2.4 20 ml of 1,4-butanediol in a 50 ml three-necked flask at room temperature for reaction at 220 1C for 0.5 h (Table 1). The synthetic procedure used for Rh nanocrystals was the same as that used to synthesize Pd nanocrystals, except that 0.2 mmol Rh(acac)3 was added to 20 ml of 1,4-butanediol in a 50 ml three-necked flask at room temperature and evacuated at 140 1C for 20 min, followed by reaction at 205 1C for 2 h (Table 1). (2) Preparation of the Langmuir–Blodgett film The Rh1 xPdx nanocrystals were washed several times by repeated cycles of precipitation and dispersion. Precipitation was performed by adding 1 ml of the nanocrystal solution to 4 ml of hexane. The supernatant was decanted and the remaining precipitated nanoparticles were dispersed by sonication in 1 ml of ethanol (in early wash cycles) or chloroform (in later wash cycles) to remove the impurities and excess PVP. Monolayer of Rh1 xPdx nanocrystals was formed by placing drops of Rh1 xPdx nanocrystal chloroform solution onto the water surface of a LB trough (Nima Technology, M611) at room temperature.18 The surface pressure was monitored with a Wilhelmy plate, which was adjusted to zero prior to spreading the nanocrystals. The resulting surface layer was compressed by moving the mobile barrier at a rate of 15 cm2 min 1. A typical surface pressure was 11 mN m 1, which resulted in nanoparticle surface coverage of 15–30%. The Rh1 xPdx nanocrystals were deposited onto Si wafers (1 cm 1 cm) by lift-up of the substrates at a rate of 1 mm min 1 using the Langmuir–Schäffer horizontal liftoff method. This 2D sample geometry was used for reaction studies and the APXPS studies. (3) CO oxidation reactions at atmospheric (760 Torr) and moderate (100–200 mTorr) pressure CO oxidation reactions were performed using two setups: one atmospheric-pressure setup, and one moderate-pressure setup. The first setup was used to obtain turnover frequency (TOF) and activation energy using gas chromatography (GC) at a total pressure of one atmosphere. The second setup was used to obtain light-on temperatures and qualitative comparison of reaction rates at total pressures of 100–200 mTorr. This setup was built specifically to mimic the conditions used in APXPS studies of surface segregation and oxidation behavior in bimetallic nanoparticle catalyst systems, such as Rh1 xPdx catalysts,17 in order to bridge the pressure gap between conventional kinetic studies and photoelectron-based studies. The atmospheric-pressure setup consisted of a laboratory scale batch reactor with continuous gas recirculation between 160 and 200 1C. Samples were loaded into quartz reactors with a type-K thermocouple touching the reactor near the sample. Prior to the reaction, the manifold was filled with 40 Torr CO (Praxair, UHP), 100 Torr O2 (Praxair, UHP), and a balance of He (Praxair, UHP) initially at atmospheric pressure, all regulated by mass flow controllers. Gas composition was analyzed with a HP 5890 Series II gas chromatograph equipped with a thermal conductivity (TCD) detector. Turnover frequency (reported as product molecules site 1 s 1) was calculated by extrapolating the conversion data to the initial Phys. Chem. Chem. Phys., 2011, 13, 2556–2562 2557 Published on 24 December 2010. Downloaded by Iowa State University on 07/12/2015 20:26:49. View Article Online time and by correcting the Rh1 xPdx surface area using the method described above. The moderate-pressure setup, in contrast, uses a twochamber system in order to feed very small pressures of the reaction gas mixture to a low-pressure chamber for detection. Reactants are fed to a high-pressure reaction chamber (0.3 L) using two leak valves—one for O2 and one for CO. The contents of the high-pressure chamber are sampled into a low-pressure chamber through a leak valve. The low-pressure chamber is kept at a pressure of 5 10 8 Torr using a turbomolecular pump. Reactant and product concentration is measured using a mass spectrometer (Stanford Research Systems) in the low-pressure chamber. Sample temperature is controlled using a ceramic button heater (Momentiv), and a type-K thermocouple. Gas mixing was found to be very efficient and changes in the reaction chamber are registered by the mass spectrometer almost immediately. The system functions similarly to a batch reactor due to the low flow rate of gas in and out of the reaction chamber. (4) APXPS studies APXPS was carried out on the Scienta 4000-HiPP endstation at beamline 9.3.2 of the Advanced Light Source.19 A Rh0.5Pd0.5, pure Rh, and pure Pd sample were mounted together on a 1 cm button heater. Pd 3d, Rh 3d, C 1s, and Si 2p spectra were monitored at 490 eV photon energy for all three samples as the O2 pressure, CO pressure, and temperature were varied. At each pressure/temperature condition, the Pd 3d/Rh 3d ratio was monitored until it reached steady state, typically after 3 h at each condition. Characterization of the RhPd bimetallic nanoparticles The size, shape, and lattice structure of the Rh1 xPdx nanocrystals were analyzed using a Philips FEI Tecnai 12 transmission electron microscope (TEM) and Philips CM200/FEG highresolution TEM (HRTEM), operated at 100 kV and 200 kV, respectively. The samples were prepared by placing a drop of the nanocrystal solution in ethanol onto a continuous carboncoated copper TEM grid. Powder X-ray diffraction (XRD) patterns were recorded on a Bruker D8 GADDS diffractometer using Co-Ka radiation (l = 1.79 Å). Lattice parameters of the nanocrystals were calculated with the least-squares method. X-Ray Photoelectron Spectroscopy (XPS) experiments were performed on a Perkin-Elmer PHI 5300 XPS spectrometer with a position-sensitive detector and a hemispherical energy analyzer in an ion-pumped chamber (evacuated to 2 10 9 Torr). The Al-Ka (1486.6 eV) X-ray source of the XPS spectrometer was operated at 350 W with a 15 kV acceleration voltage. XPS was also carried out in UHV at the Advanced Light Source Beamline 9.3.2 for energydependent (and therefore depth-dependent) composition analysis. This system has been described previously.17 The binding energy (BE) for the samples was calibrated by setting the measured BE of the broad C 1s, which is dominated by carbon from the PVP capping agent, to 285 eV. The elemental ratio was calculated from the integrated peak areas of the Rh 3d, Pd 3d, and O 1s core levels. The morphological changes of 2558 Phys. Chem. Chem. Phys., 2011, 13, 2556–2562 the Rh1 xPdx nanocrystals, Rh thin films, and Pd thin films before and after reaction were observed with a Zeiss Gemini Ultra-55 analytical scanning electron microscope (SEM). The total number of surface sites was calculated from coverage determined by a minimum of ten SEM images taken from randomly selected locations on each sample and taking into account the lattice parameters determined from XRD. This calculation is purely geometric and does not account for site blocking by strongly-bound capping agent molecules or other species. Panels a–f of Fig. 1 display TEM images of the Rh1 xPdx (x = 0–0.8) nanocrystals. The bimetallic nanocrystals are faceted, but show a mix of various shapes in 2D projection, such as hexagons, pentagons, triangles, and cubes. All the bimetallic nanocrystals have an average crystallite size near 15 nm, with standard size distributions of around 15% (Table 1). XRD measurements determined that all the bimetallic nanocrystals have a face-centered cubic (fcc) structure with lattice parameters lying between 0.385 and 0.397 nm (Table 1). The surface compositions and structure of the bimetallic nanocrystals were measured experimentally by XPS in ultrahigh vacuum. Two systems were used—one system with an Al K-a source with X-ray Photon Energy of 1486.6 eV (photoelectron mean free path B1.6 nm) and another system with a tunable synchrotron source set to 645 eV (photoelectron mean free path B0.7 nm). As shown in Fig. 2, the atomic fraction of Pd is significantly lower at the surface of the bimetallic nanoparticles than in the bulk. This demonstrates that the as-synthesized nanoparticles have clear core–shell geometry, with a Pd-rich core and Rh-rich shell. The transition between these regions is gradual and comprised of mixed Rh–Pd phases. Changes in the local chemical environment dramatically affect the surface composition and oxidation state of the nanocrystals by inducing selective phase-segregation of the nanoparticle components.17 Reaction and APXPS results and discussion CO oxidation tests in 40 Torr CO, 100 Torr O2 and 620 Torr He using the atmospheric-pressure reactor revealed that all the bimetallic nanocrystals are active for CO oxidation between 170–210 1C. SEM measurements before and after reaction showed that no severe aggregation occurred, as shown in Fig. 3. The turnover frequency was strongly dependent on nanoparticle composition, as shown at 180 1C and 190 1C in Fig. 4a. The maximum turnover frequency was 1.34 molecules site 1 s 1 at 190 1C on the Rh0.6Pd0.4 nanocrystals. Turnover frequencies were also compared to the theoretical activity of a linear combination of pure Rh and pure Pd nanocrystals, x)) + calculated as TOFLinear-combination = (TOFRh (1 (TOFPd x). The maximum measured enhancement was 5.0 at 180 1C for the Rh0.2Pd0.8 nanocrystals versus the theoretical activity of a linear combination of pure Rh and pure Pd nanoparticles. The enhancement factor decreased with increasing temperature for all samples. The CO oxidation reaction was also carried out at in both a mixture of 100 mTorr O2 and 40 mTorr CO, and a mixture of 100 mTorr O2 and 100 mTorr CO. Rh and Rh0.5Pd0.5 nanoparticles were both very active in these conditions, while the This journal is c the Owner Societies 2011 Published on 24 December 2010. Downloaded by Iowa State University on 07/12/2015 20:26:49. View Article Online Fig. 1 TEM images and size distribution histograms (insets) of Rh1 xPdx nanocrystals: (a) x = 0; (b) x = 0.2; (c) x = 0.4; (d) x = 0.5; (e) x = 0.6; (f) x = 0.8. Pd nanoparticles had a very low turnover frequency. The turnover frequency measured from each nanoparticle catalyst at 175 1C and 100 mTorr O2 in 40 mTorr CO and 100 mTorr CO is compared in Fig. 4b. At 175 1C in 100 mTorr O2 and 40 mTorr CO, the Rh nanoparticles had a turnover frequency of 0.078 molecules site 1 s 1, as compared to a turnover frequency of 0.211 molecules site 1 s 1 for the Rh0.5Pd0.5 nanoparticles and a turnover frequency of 0.0018 molecules site 1 s 1 for the Pd nanoparticles. These turnover frequencies are lower than those measured at high pressure, as expected from entropic considerations. Notably, the turnover frequency measured on the bimetallic nanoparticles was significantly larger than on either the Rh or Pd monometallic nanoparticles. The maximum measured enhancement was 5.3 for the Rh0.5Pd0.5 nanoparticles versus the theoretical activity of a linear combination of pure Rh and pure Pd nanocrystals in these conditions. Apparent activation energy was measured both at atmosphere and low pressure, which showed strong dependence This journal is c the Owner Societies 2011 on nanoparticle composition. At atmosphere pressure, it decreased with increased Pd molar fraction, from a maximum of 108 kcal mol 1 for pure Rh to a minimum of 51 kJ mol 1 for pure Pd nanoparticles. This trend is consistent with studies on pure Rh and Pd nanoparticles.20,21 At low pressure (100 mTorr O2 and 100 mTorr CO), the apparent activation energy measured for the bimetallic nanoparticles followed the same trend as those obtained at atmosphere pressure. The turnover frequencies measured using bimetallic nanoparticles were greater than those measured on the monometallic nanoparticles. This indicates that the enhancement effect is too large to be explained simply by complete coverage of the nanoparticle surface with Rh. Consequently, the synergetic effect must be due to interaction between Rh and Pd or their adsorbates. These results are consistent with previous studies, which found synergistic behavior in Rh–Pd catalysts prepared by sequential impregnation and co-impregnation7,16,22,23 and lower ignition temperature for Rh nanoparticle catalysts as Phys. Chem. Chem. Phys., 2011, 13, 2556–2562 2559 Published on 24 December 2010. Downloaded by Iowa State University on 07/12/2015 20:26:49. View Article Online Fig. 2 Pd atomic fraction of the Rh1 xPdx nanocrystals in UHV determined at X-ray energies of 1486.6 eV and 645 eV by XPS versus as-synthesized total Pd composition. The X-ray with higher energy can probe deeper surface than that with lower energy. For RhPd bimetallic nanoparticle, the 645 eV X-ray can only probe less than 0.7 nm surface, and thus are very surface sensitive. These results clearly demonstrated that the bimetallic nanoparticles posses a Rh rich surface. Fig. 3 SEM images of Rh0.6Pd0.4 nanocrystals (a) before and (b) after CO oxidation. No obvious particle aggregation is observed after CO oxidation. compared to Pd nanoparticle catalysts studied in similar conditions.23–25 Previous studies also determined that synergism does not occur in physical mixtures in this system.23,26 To better understand the mechanism of the observed synergetic effect, we used APXPS to study the surface composition and the oxidation state of Pd and Rh under reaction conditions. The as-synthesized Rh0.5Pd0.5 nanoparticles have a Rh rich surface (Fig. 2). When we first introduce 100 mTorr O2 and 40 mTorr CO at 175 1C, the surface composition of Pd increased slightly from 10% to 11%. When the CO pressure was increased to 100 mTorr, the surface Pd increased to 23%, which indicates that CO has a stronger interaction with Pd than with Rh. Further evidence for the stronger interaction of O2 with Rh and CO with Pd was observed by exposing the NPs to 100 mTorr O2 or 100 mTorr CO separately or to a mixture of 100 mTorr of both gases. The Pd 3d and Rh 3d spectra are shown in Fig. 5. Rh 3d is 70% oxidized in pure O2 while Pd 3d is only 29% oxidized. In pure CO, however, the Pd 3d peak shows increased intensity at higher BE, indicating a strong interaction with CO or dissociated C atoms. It is possible, then, that the preferential adsorption of CO on isolated Pd atoms could lead directly to the synergetic increase 2560 Phys. Chem. Chem. Phys., 2011, 13, 2556–2562 Fig. 4 (a) Turnover frequency at 180 1C and 190 1C as a function of Pd molar fraction for Rh1 xPdx nanocrystals in 100 Torr O2, 40 Torr CO, 620 Torr He. Dashed lines represent the theoretical activity of a linear combination of pure Rh and pure Pd nanocrystals. A significant synergetic effect was observed for the bimetallic catalysts in these reaction conditions. (b) Turnover frequency in 100 mTorr O2 and 175 1C versus CO pressure and Pd molar fraction for Rh1 xPdx bimetallic nanoparticle catalysts. Dashed lines represent the theoretical activity of a linear combination of pure Rh and pure Pd nanocrystals. The degree of the synergetic effect observed for the bimetallic catalyst increased with O2 to CO ratio. Fig. 5 (a) Pd 3d and (b) Rh 3d spectra from Rh0.5Pd0.5 NPs at 220 1C in 100 mTorr O2 (red), 100 mTorr CO (blue) and a reaction mixture of nominally 100 mTorr O2 + 100 mTorr CO (black). In pure CO, the Pd 3d peak shows increased intensity at higher BE, indicating a strong interaction with CO or dissociated C atoms. In pure O2, however, the Rh 3d indicates a large degree of oxidation (approximately 70%) while the Pd 3d indicates only a relatively modest degree of oxidation (29%). in the reaction rate observed because isolated Pd on the Rh-dominated surface ensures an adequate supply of adsorbed CO for the reaction while oxygen dissociatively adsorbs on Rh. In this model, the reaction rate is increased by reaction at Pd sites between oxygen spillover from Rh and the CO-covered Pd sites. In this case, the synergetic effect is This journal is c the Owner Societies 2011 View Article Online Published on 24 December 2010. Downloaded by Iowa State University on 07/12/2015 20:26:49. our high pressure work, which was carried out at an intermediate PO2/PCO ratio, found an intermediate synergetic enhancement, and our low pressure work found a significantly higher enhancement when PO2/PCO = 2.5 than when PO2/PCO = 1 under otherwise-identical conditions. It is important to note that this correlation is independent of reaction order because these enhancements are relative to linear combinations of pure Pd and pure Rh catalyst activity. Fig. 6 (a) Pd 3d and (b) Rh 3d spectra from Rh0.5Pd0.5 NPs at 175 1C in reaction mixtures of nominally 100 mTorr O2 + 100 mTorr CO (red) and 100 mTorr O2 + 40 mTorr CO (black). At 175 1C in the mixtures of 100 mTorr O2 and 40 mTorr CO, the surface was 26% Pd. Upon increasing the CO pressure back to 100 mTorr, the surface Pd increased to 31%. This indicates that at higher oxygen pressures, Pd sites are increasingly isolated on an ever more Rh-dominated surface for the Rh0.5Pd0.5 nanoparticles. heavily dependent on the distribution of Rh and Pd in the top layers. This observation also supports the mechanism originally proposed for Rh–Pt by Oh and Carpenter26 and later extended to Rh–Pd by Araya and Diaz,7 that surface oxygen from RhOx species may react with CO adsorbed on reduced Pt atoms. In order to gain a better understanding of the equilibrium Rh/Pd ratio under these reaction conditions, the NPs were heated to 220 1C in 100 mTorr O2 + 100 mTorr CO for 3 hours, followed by checking again the original conditions of 100 mTorr O2 + 40 mTorr CO at 175 1C and then increasing the CO pressure to 100 mTorr. After 3 hours at 220 1C in 100 mTorr O2 + 100 mTorr CO, the surface Pd increased to 30%. After decreasing the CO pressure to 40 mTorr and the temperature to 175 1C, the surface was only 26% Pd. Upon increasing the CO pressure back to 100 mTorr, the surface Pd again increased to 31% (Fig. 6). This indicates that at higher relative oxygen pressures, Pd sites are increasingly isolated on an ever more Rh-dominated surface for the Rh0.5Pd0.5 nanoparticles. It is also evident from Fig. 6 that at lower CO pressure, the Rh 3d peak shifts to higher BE (approximately 8% oxidized), while the Pd 3d peak does not shift (no oxidation). This observation further supports our claim that more RhOx species form at higher PO2/PCO ratio, leading to an enhanced synergistic effect. Both the formation of RhOx species and the decreased surface Pd content may contribute to the enhanced synergistic effect with increasing PO2/PCO ratios. The measured enhancements in both this study and similar studies by Yoon et al.23 and Araya and Weissman16 are consistent with the APXPS observations. In each study, the PO2/PCO is different and the measured enhancement changes as we would predict. Our reaction, as previously stated, was carried out in PO2/PCO = 2.5 at 180 1C and 190 1C at high pressure, and PO2/PCO = 2.5 and 1 at 175 1C, while Weissman et al.’s study was carried out at PO2/PCO = 5 at 135 1C and Yoon et al.’s study was in PO2/PCO = 1 at 180 1C. Weissman et al.’s study, which had the highest PO2/PCO ratio, also found the highest synergetic enhancement, while Yoon et al.’s study, with the lowest PO2/PCO ratio, found the lowest synergetic enhancement. The present study confirms this correlation, as This journal is c the Owner Societies 2011 Conclusions Rh1 xPdx nanocrystals or 15 nm in diameter were synthesized, characterized, and studied in catalytic CO oxidation in two pressure regimes. A model based on APXPS studies was proposed to help explain the observed catalytic behavior. The nanocrystals were found to exhibit significant compositiondependent synergetic effects in CO oxidation. This observed synergy could be related to preferential adsorption of CO on isolated Pd atoms or islands on the bimetallic catalyst surface and spillover of oxygen adsorbates from Rh to CO-covered Pd reaction sites. Our APXPS and reaction results resolve questions arising from discrepancies in the degree of synergetic enhancement measured on bimetallic nanoparticles in the CO oxidation reaction by demonstrating a clear correlation between the O2 : CO ratio, surface composition and bimetallic nanoparticle synergy. This unique and desirable synergetic behavior in bimetallic catalysts will hopefully lead to greater understanding of the many complex factors governing reactivity in these systems. Acknowledgements This work was supported by the Director, Office of Science, Office of Basic Energy Sciences, of the U.S. Department of Energy under Contract No. DE-AC02-05CH11231. Y.W.Z. gratefully acknowledges the financial aid of Huaxin Distinguished Scholar Award from Peking University Education Foundation of China. References 1 V. R. Stamenkovic, B. Fowler, B. S. Mun, G. F. Wang, P. N. Ross, C. A. Lucas and N. M. Markovic, Science, 2007, 315, 493–497. 2 F. Gao, Y. L. Wang and D. W. Goodman, J. Phys. Chem. C, 2009, 113, 14993–15000. 3 S. A. Giraldo, M. H. Pinzon and A. Centeno, Catal. Today, 2008, 133, 239–243. 4 Q. Shen, L. D. Li, Z. P. Hao and Z. P. Xu, Appl. Catal., B, 2008, 84, 734–741. 5 J. G. Zhang, H. Wang and A. K. Dalai, J. Catal., 2007, 249, 300–310. 6 Y. W. Zhang, W. Y. Huang, S. E. Habas, J. N. Kuhn, M. E. Grass, Y. Yamada, P. Yang and G. A. Somorjai, J. Phys. Chem. C, 2008, 112, 12092–12095. 7 P. Araya and V. Diaz, J. Chem. 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