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Haoxiong Nan, Xinlong Tian, Lijun Yang, Ting Shu, Huiyu Song, Shijun Liao, "A Platinum Monolayer Core-Shell Catalyst with a Ternary Alloy Nanoparticle Core and Enhanced Stability for the Oxygen Reduction Reaction", Journal of Nanomaterials, vol. 2015, Article ID 715474, 11 pages, 2015. https://doi.org/10.1155/2015/715474
A Platinum Monolayer Core-Shell Catalyst with a Ternary Alloy Nanoparticle Core and Enhanced Stability for the Oxygen Reduction Reaction
We synthesize a platinum monolayer core-shell catalyst with a ternary alloy nanoparticle core of Pd, Ir, and Ni. A Pt monolayer is deposited on carbon-supported PdIrNi nanoparticles using an underpotential deposition method, in which a copper monolayer is applied to the ternary nanoparticles; this is followed by the galvanic displacement of Cu with Pt to generate a Pt monolayer on the surface of the core. The core-shell Pd1Ir1Ni2@Pt/C catalyst exhibits excellent oxygen reduction reaction activity, yielding a mass activity significantly higher than that of Pt monolayer catalysts containing PdIr or PdNi nanoparticles as cores and four times higher than that of a commercial Pt/C electrocatalyst. In 0.1 M HClO4, the half-wave potential reaches 0.91 V, about 30 mV higher than that of Pt/C. We verify the structure and composition of the carbon-supported PdIrNi nanoparticles using X-ray powder diffraction, X-ray photoelectron spectroscopy, thermogravimetry, transmission electron microscopy, and energy dispersive X-ray spectrometry, and we perform a stability test that confirms the excellent stability of our core-shell catalyst. We suggest that the porous structure resulting from the dissolution of Ni in the alloy nanoparticles may be the main reason for the catalyst’s enhanced performance.
Although proton exchange membrane fuel cells (PEMFCs) are recognized as a promising form of technology to meet the global energy crisis and address various associated environmental problems, many technical and economic challenges prevent their large-scale commercialization, one of which is the high cost of platinum . Despite the fact that numerous efforts have been paid to search for substitute materials for platinum, such as Pd , Ir , Ag , Au , Fe- and N-doped carbon catalyst , and carbon nanotube/Fe3C nanoparticle , a platinum-based catalyst is still the best choice for oxygen reduction in an acidic environment. In recent years, the emergence of core-shell catalysts [8–12], especially those with a Pt monolayer [13–20], has brought PEMFC commercialization closer to becoming a reality, because the mass activity of Pt in a core-shell catalyst can be enhanced by several times. However, most current core-shell catalysts still use precious metals (such as Pd [21, 22]) as the cores, and this makes it difficult to reduce the cost of catalysts effectively. To address this problem, some studies have introduced nonprecious metals into the alloy nanoparticles, yielding cores such as PdCo, PdNi, and PdFe [23–25]. However, catalyst stability has remained a problem. Kuttiyiel et al. reported that an electrocatalyst’s stability could be significantly enhanced by adding a negligible amount of Au to the PdNi nanoparticle core . Knupp et al. found that the stability of a Pd@Pt/C catalyst could be improved by adding iridium to the Pd core .
In this study, we prepared a Pt monolayer core-shell catalyst with a ternary PdIrNi alloy nanoparticle as the core using an underpotential deposition (UPD) method. As expected, this catalyst exhibited superior oxygen reduction reaction (ORR) activity to a commercial Pt/C catalyst as well as enhanced stability.
2.1. Preparation of Carbon-Supported PdIrNi Nanoparticles
The carbon-supported ternary alloy nanoparticles were prepared as follows. Palladium chloride, iridium chloride, and nickel chloride in an atomic ratio of 1 : 1 : 2 were added to deionized water to obtain a solution. Next, sodium citrate was added as a complexing agent using a metal/citrate molar ratio of 1 : 5, after which carbon black XC-72R was added to the solution under strong stirring. After the mixture was purged with high-purity N2 for 15 minutes, excess NaBH4 solution (10 wt%) was slowly added, using ultrasonication and under the protection of nitrogen. After reaction with ultrasonication for one hour, the mixture was filtered and washed with deionized water three to five times and then dried overnight in a vacuum oven at 50°C. For comparison, binary nanoparticles of PdNi, IrNi, and PdIr were prepared using the same procedures. The metal content in each of the samples was 20 wt%.
2.2. Synthesis of Core-Shell Catalyst on Glassy Carbon Electrode by UPD
The Pt monolayer core-shell catalyst PdIrNi@Pt/C was prepared on a glassy carbon electrode using a UPD method. First, 5.0 mg carbon-supported ternary PdIrNi alloy nanoparticles were dispersed in 1 mL Nafion ethanol solution (0.1 wt%) via ultrasonication for 30 minutes to make a uniform suspension. Then, 5 μL of the suspension was pipetted onto a glassy carbon disk electrode (5 mm diameter) and dried in air. Next, a Cu monolayer was deposited on the surface of the PdIrNi nanoparticles in a 0.05 M H2SO4 + 0.05 M CuSO4 solution by holding the deposition potential at about 0.37 V for one minute, under the protection of high-purity nitrogen. Finally, the electrode was transferred into a solution of 1 mM K2PtCl4 + 0.05 M H2SO4 for 10 minutes in a nitrogen atmosphere, in which the Cu monolayer was galvanically replaced by Pt to form a Pt monolayer. The theoretical Pt content in the catalyst was calculated from the UPD charge of Cu, and the real content was determined by inductively coupled plasma-atomic emission spectrometry (ICP-AES).
This prepared electrode bearing the core-shell structured catalyst was used for the subsequent electrochemical performance measurements without further treatment.
2.3. Measurement of the Catalysts’ Electrochemical Performance
The electrochemical performance of the catalysts was measured by cyclic voltammetry (CV) on an electrochemical workstation (Ivium, Netherlands) using a three-electrode electrochemical cell. An Ag/AgCl/KCl (3 M) leak-free reference electrode and a Pt wire were used as the reference and counter electrodes, respectively. ORR and hydrogen underpotential deposition (HUPD) measurements were performed in 0.1 M HClO4 solution saturated with oxygen and nitrogen at room temperature.
2.4. Catalyst Characterization
X-ray powder diffraction (XRD) patterns were obtained with a TD-3500 powder diffractometer (Tongda, China) using filtered Cu-Kα radiation operating at 40 kV and 30 mA. Scanning transmission electron microscope (STEM) images were recorded on a JEOL JEM 2100F operated at 200 kV. Thermogravimetric (TG) analyses were performed on a Q600 SDT analyzer (TA Inc., USA) in a pure nitrogen flow (100 mL min−1) at a heating rate of 10°C min−1 from room temperature to 950°C. X-ray photoelectron spectroscopy (XPS) was performed on an Axis Ultra DLD X-ray photoelectron spectrometer (Kratos, England) employing a monochromated Al-Kα X-ray source (hν = 1486.6 eV). ICP-AES (Leema PROFILE, America) was used to analyze the contents of trace metal elements.
3. Results and Discussion
The structures of the as-prepared catalysts were characterized by XRD (Figure 1). The first peak, located at about 23.2°, refers to the Vulcan XC72 carbon support. The diffraction peaks at the 2θ values of 42.5° for the PdIrNi/C catalysts readily correspond to the (111) crystal planes of the face-centered cubic crystalline structure. As shown in Figure 1(a), the (111) diffraction peak of Pd1Ir1Ni2@Pt/C has shrunk sharply and shifted negatively slightly (about 0.8°) compared to that of Pd1Ir1Ni2/C; we suggest this is due to the dissolution of Ni from the alloy nanoparticles during the UPD process, and the results of the ICP-AES analysis confirm this explanation.
It should be pointed out that no diffraction peaks corresponding to Pt could be observed in the XRD pattern of Pd1Ir1Ni2@Pt/C, perhaps because the Pt monolayer could not generate diffractions.
It is interesting that no diffraction peaks of Ni and Ir could be observed for the Pd1Ir1Ni2/C sample, even though the Ni and Ir contents were up to 50 at % and 25 at %, respectively. There may be two reasons: (1) the Ni atoms entered the Pd lattice to form a complete alloy; (2) Ni formed an X-ray amorphous phase that will not be observed in the diffractogram. Figure 1(b) shows the XRD patterns of the PdIrNi/C catalysts with a Pd/Ir ratio of 1 and various Pd/Ni ratios. The lattice parameters of Pd1Ir1/C, Pd2Ir2Ni1/C, Pd1Ir1Ni2/C, and Pd1Ir1Ni8/C were 3.873, 3.783, 3.688, and 3.681 Å calculated from the (111) diffraction plane by Jade software. The atomic radii of Pd, Ir, and Ni atoms are 1.37, 1.36, and 1.25 Å, respectively. When more Ni atoms entered into the Pd lattice, it can result in the decrease of the lattice parameter and the Pd–Pd interatomic distance because the radius of the Ni atom was smaller than that of the Pd atom . Clearly, the (111) diffraction peak for the catalysts shifted positively as the Ni content increased, and the lattice parameters decreased obviously with the increase of the content of nickel.
Figure 2 presents TEM images of the Pd1Ir1/C, Pd1Ir1@Pt/C, Pd1Ir1Ni2/C, and Pd1Ir1Ni2@Pt/C catalysts. It can be observed that all of the nanoparticles were well dispersed on the carbon support without apparent aggregation either before or after the Pt deposition. The Pd1Ir1/C and Pd1Ir1Ni2/C nanoparticles exhibited a rather narrow size distribution, in the range of 1–3.5 and 1.25–2.5 nm, with average diameters of about 2.2 and 1.7 nm, respectively, which are in agreement with the particle results predicted by XRD. On the basis of the high-resolution TEM (HRTEM) shown in Figures 2(b) and 2(f), there was a decrease of the lattice distance for Pd1Ir1Ni2/C (0.22 nm) compared to that of Pd1Ir1/C (0.225 nm), which can be explained by the addition of Ni. XRD measurements also demonstrated that lattice contraction occurred, as the (111) diffraction peak of Pd1Ir1Ni2/C showed a slight positive shift compared to that of Pd1Ir1/C. The smaller size and better dispersion observed for Pd1Ir1Ni2/C in comparison to Pd1Ir1/C can be attributed to the addition of Ni to the alloy.
After the deposition of Pt, the Pd1Ir1@Pt/C and Pd1Ir1Ni2@Pt/C catalysts showed average diameters of ~2.85 and ~2.30 nm, respectively (see the size distributions provided in Figures 2(c) and 2(g)). The diameters of both nanoparticles increased by ca. 0.6 nm, indicating that the thickness of the Pt shell layer was ca. 0.3 nm, corresponding to a monolayer of Pt atoms. These results confirm the core-shell structure of Pd1Ir1@Pt/C and Pd1Ir1Ni2@Pt/C. To obtain a better distribution of Pd, Ir, Ni, and Pt in Pd1Ir1Ni2@Pt/C, we employed high-angle annular dark field (HAADF) imaging and conducted a line-profile analysis using STEM/energy dispersive spectroscopy (EDS). As shown in Figures 2(i) and 2(j), the profile analysis revealed a lower intensity of Pt at the center than at the PdIrNi edges, suggesting the formation of a core (PdIrNi)/shell (Pt) structure. The lattice distances were found to be 0.217 nm for Pd1Ir1@Pt/C and 0.215 nm for Pd1Ir1Ni2@Pt/C (Figures 2(d) and 2(h)), compared to 0.225 and 0.22 nm for Pd1Ir1/C and Pd1Ir1Ni2/C, respectively. The decrease of interplanar spacing was caused by the force between the core and the Pt shell.
The elements on the surfaces of the Pd1Ir1Ni2/C, Pd1Ir1Ni2@Pt/C, and Pt/C catalysts were characterized by XPS. Figures 3(a) and 3(b) show the XPS survey spectra, and Figures 3(c)–3(h) show the Pd 3d, Ir 4f, and Pt 4f XPS spectra of Pd1Ir1Ni2/C, Pd1Ir1Ni2@Pt/C, and Pt/C. The binding energy was calibrated by means of the C 1s peak energy of 284.56 eV. The results, given as percentages of total intensity, are presented in Table 1. It can be seen that Pd1Ir1Ni2@Pt/C showed a decrease in Pd 3d and Ir 4f concentrations compared to Pd1Ir1Ni2/C, even though the Pd/Ir ratio was almost unchanged. Ni was not detected in the Pd1Ir1Ni2@Pt/C nanoparticles for two main reasons: first, most of the Ni nanoparticles leached out from the Pd1Ir1Ni2/C; second, the strong F Auger (833.0 eV) covered the peak of the Ni nanoparticles. The best fits of the Pd (0) 3d spectra (Figure 3(a)) were obtained using two doublets (Pd 3d5/2 and 3d3/2) with a fixed doublet separation (DS = 5.2 eV). This method revealed that the binding energy of Pd (0) 3d (336.5 and 341.7 eV) in Pd1Ir1Ni2@Pt/C experienced a positive shift of 0.3 eV compared with that of Pd1Ir1Ni2/C (336.19 and 341.35 eV), and the binding energy of Ir (0) 4f (61.58 and 62.79 eV) in Pd1Ir1Ni2@Pt/C underwent a positive shift of 0.2 eV compared with that of Pd1Ir1Ni2/C (61.39 and 62.6 eV). What is more, a clear negative shift of ca. 0.3 eV in the binding energy of Pt 4f for Pd1Ir1Ni2@Pt/C catalyst with respect to the 20% JM-Pt/C catalyst can be observed. These observations further confirmed the electron interactions involving the alloy core and Pt atoms within the Pd1Ir1Ni2@Pt/C catalyst. The negative shift of the Pt 4f binding energy implied that the Pt nanoparticles can get electrons from the alloy core, leading to a weakened interaction between intermediate oxide species and Pt atoms that the ORR was improved .
3.2. Oxygen Reduction Reaction
Figure 4(a) shows the CV curves for Pd1Ir1Ni2/C, Pd1Ir1Ni2@Pt/C, Pd1Ir1/C, and Pd1Ir1@Pt/C in deaerated 0.05 M H2SO4 at a scan rate of 50 mV s−1. Pd1Ir1Ni2/C and Pd1Ir1/C clearly exhibited almost the same CV curves, apart from the slight positive shift in the position of the metal oxide reduction peak in Pd1Ir1Ni2/C; both had almost the same hydrogen reduction and oxidation peaks. Conversely, it is interesting that, in the case of Pd1Ir1@Pt/C and Pd1Ir1Ni2@Pt/C, Pd1Ir1@Pt/C exhibited obviously larger hydrogen reduction and oxidation peaks than Pd1Ir1Ni2@Pt/C, and the reduction peaks of the surface metal oxide shifted from ca. 0.7 V to ca. 0.8 V, clearly confirming that Pt was covering the core nanoparticles. It is important that the electrochemical surface area (ECSA) of Pd1Ir1@Pt/C (147.7 m2 g−1 Pt) was higher than that of Pd1Ir1Ni2@Pt/C (114.5 m2 g−1 Pt); however, the mass activity of Pd1Ir1Ni2@Pt/C was higher than that of PdIr@Pt/C, as we will discuss later. As shown in Figure 4(b), the deposition reduction peak and oxidation peak related to the Cu UPD can be observed on the Pd1Ir1/C and Pd1Ir1Ni2/C clearly. It is found that the peak area of Pd1Ir1/C was higher than that of Pd1Ir1Ni/C. The theoretical Pt contents in Pd1Ir1@Pt/C and Pd1Ir1Ni2@Pt/C catalysts by calculating from the UPD charge of Cu were 6.31 μg cm−2 and 5.21 μg cm−2, respectively.
Figure 5 shows the ORR polarization curves of Pd1Ir1@Pt/C, Pd1Ir1Ni2@Pt/C, IrNi@Pt/C, PdNi@Pt/C, and 20% JM-Pt/C at 1600 rpm in oxygen-saturated 0.1 M HClO4 solution. The Pd1Ir1Ni2@Pt/C exhibited the best ORR activity, even superior to that of commercial 20% JM-Pt/C. The Pt loading of Pd1Ir1Ni2@Pt/C was 5.24 nmol (5.22 μg cm−2), and the PdIr loading was 24 nmol (18.29 μg cm−2). The electrocatalyst’s considerable activity was indicated by the high onset potential of O2 reduction (0.9–1.05 V) as well as by the high half-wave potential (885 mV at a rotation rate of 1600 rpm). The mass activity of Pd1Ir1Ni2@Pt/C was 1.5 times that of Pd1Ir1@Pt/C and over four times that of commercial 20% JM-Pt/C. Based on these results, we can conclude that (1) the high mass activity of Pd1Ir1Ni2@Pt/C may be strong evidence for the formation of a core-shell structured catalyst and (2) the addition of Ni may have played an important role in performance enhancement.
To further understand this excellent mass activity enhancement and the role of Ni, we measured the real composition of all the catalysts, as shown in Table 2. For Pd1Ir1Ni2@Pt/C and Pd1Ir1@Pt/C, the actual Pt contents were close to their theoretical contents: the deviations were ~3.5% for Pd1Ir1Ni2@Pt/C and ~13.7% for Pd1Ir1@Pt/C. For all of the samples containing Ni, we found that the Ni was almost totally removed during the scanning and UPD steps; for Pd1Ir1Ni2@Pt/C, the Ni residue was only 0.05 μg μg−1 catalyst, which was just 0.05% of the Ni in the Pd1Ir1Ni2/C sample, indicating 99.5% of the Ni had been removed during the UPD process . Clearly, Pd1Ir1Ni2@Pt/C contained less deposited Pt than Pd1Ir1@Pt/C, and the UPD step removed the Ni, so why did Pd1Ir1Ni2@Pt/C exhibit higher mass activity than Pd1Ir1@Pt/C? Since the lower Pt loading of Pd1Ir1Ni2@Pt/C indicates that Ni was not replaced with Pt, we suggest that the porous structure created by the dissolution of Ni may be the reason for the enhanced mass activity of Pd1Ir1Ni2@Pt/C.
Figure 6 shows the ORR polarization curves of the catalysts containing various amounts of Ni and of 20% JM-Pt/C at 1600 rpm in oxygen-saturated 0.1 M HClO4. These results confirm that Pd1Ir1Ni2@Pt/C exhibited the best ORR performance, implying that higher or lower Ni content may not be beneficial.
Figure 7(a) shows the rotating disk electrode (RDE) measurements for the ORR on Pd1Ir1Ni2@Pt/C in oxygen-saturated 0.1 M HClO4 at different rotation speeds (400–2500 rpm). The Koutecky-Levich plots obtained from Figure 7(a) with the inverse current density as a function of the inverse of the square root of the rotation rate (ω1/2) are presented in Figure 7(b). Using the average slopes of the Koutecky-Levich plots and the equation cm2 s−1, = 1.009 × 10−2 cm2 s−1, mol L−1, is the Faraday constant, and is the geometric area of the electrode) , we calculated that the electron transfer number, , was 4.12, indicating that the ORR on Pd1Ir1Ni2@Pt/C predominantly followed the four-electron exchange pathway. Moreover, the linearity and parallelism of the plots shown in Figure 7(b) are signs of first-order kinetics with respect to molecular oxygen . The Tafel plot obtained from the kinetic current, , is shown in the inset of Figure 7(b). The plot is linear, with a slope of ~−68 mV dec−1 above 0.80 V.
Figures 7(c) and 7(d) show the ORR curves at various rotation speeds on Ir1Ni2@Pt/C, and the K–L plots derived from the curves at various potentials. From the slopes of the K–L plots, the calculated electron transfer number is 4.30, revealing that the ORR on Ir1Ni2@Pt/C also followed the four-electron transfer pathway.
The values of the Tafel slopes of Ir1Ni2@Pt/C were about −70.2 and −93.1 mV dec−1, which differ from the slope of −68 mV dec−1 obtained for Pd1Ir1Ni2@Pt/C . The latter’s lower Tafel slope may be attributed to the addition of Pd.
The Pd1Ir1Ni2@Pt/C core-shell structured catalyst exhibited excellent stability, as shown in Figure 8(a). After 10,000 CV cycles in nitrogen-saturated 0.05 mol L−1 H2SO4 solution, the ECSA decay was only 9.4%, compared to 28.1% for commercial Pt/C. Furthermore, after 10,000 ORR scans, the ORR performance of Pd1Ir1Ni2@Pt/C was almost unchanged, whilst for commercial Pt/C and home-prepared Pd@Pt catalyst the decay was 34.7% and 39.2%, respectively, indicating the outstanding stability of our core-shell structured catalyst with a Pt monolayer around a ternary alloy core.
A high-performance, highly stable core-shell structured catalyst with a Pt monolayer shell and a ternary alloy nanoparticle core has been successfully prepared via a UPD method, and the catalyst has been characterized using XRD, TEM, and XPS. The catalyst exhibited very high ORR activity and excellent stability. We found that the Ni added to the alloy played an important role in significantly enhancing the ORR performance, and we suggest that the formation of a porous structure—caused by the dissolution of Ni in the alloy nanoparticles, which left only residual Ni nanoparticles—may be the main reason for the catalyst’s enhanced performance. After 10,000 ORR scans, the half-wave potential was almost unchanged, indicating this catalyst’s outstanding stability.
Conflict of Interests
The authors declare that there is no conflict of interests regarding the publication of this paper.
This work was supported by the National Science Foundation of China (NSFC Project nos. 21276098, 21476088, 51302091, and U1301245), Ministry of Science and Technology of China (Project no. 2012AA053402), Guangdong Natural Science Foundation (Project no. S2012020011061), and Department of Education of Guangdong Province (Project no. 2013CXZDA003).
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