Supporting information. Stability Issues in Pd-based Catalysts: The Role of Surface Pt in Improving the Stability

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Supporting information Stability Issues in Pd-based Catalysts: The Role of Surface Pt in Improving the Stability and Oxygen Reduction Reaction (ORR) Activity R. K. Singh, R. Rahul, M. Neergat 1 Department of Energy Science and Engineering, Indian Institute of Technology Bombay (IITB), Powai, Mumbai, India 400076 Synthesis of Pd nanoparticles (control-experiment) We synthesized Pd nanoparticles (without hydrogen) using L-ascorbic acid as a reducing agent, i.e., Pd seed prepared without hydrogen-containing reducing agent such as NaBH 4. For a typical synthesis of Pd (without hydrogen), L-ascorbic acid (60 mg) was dissolved in water and it was heated to 80 C. Meanwhile, an aqueous solution of Pd 2+ (57 mg K 2 PdCl 4 in 3 ml water) was added drop-wise to the above solution. Then the mixture was heated for 3 h at ~80 C. The asprepared Pd nanoparticles were supported on carbon (Vulcan XC-72) to get 20 wt% precious metal loading on the carbon-support. The carbon-supported Pd nanoparticles synthesized asmentioned above was treated with 0.1 mm K 2 PtCl 4 (Pt 2+ ) solution to deposit Pt on the surface of Pd (i.e., Pt/Pd (without hydrogen)). The Pt/Pd catalyst was synthesized following the Cu deposition method reported in the literature. 13 Figs. S1 and S2 show the cyclic voltammograms (CVs) and oxygen reduction reaction (ORR) voltammograms of carbon-supported Pd (without hydrogen), Pt/Pd (without hydrogen), and Pt/Pd (synthesized by Cu deposition) in 0.1 M HClO 4 solution. The Pt/Pd (without hydrogen) shows features similar to that of Pd (without hydrogen) and their ORR voltammograms are almost comparable. On the other hand, synthesis of Pt/Pd by Cu deposition results in a better 1

coverage of Pt on Pd. The CV features of Pt/Pd (synthesized by Cu deposition) are similar to that of Pt and the half-wave potential of ORR is shifted positively by ~85 mv when compared to that of Pd (without hydrogen); ORR voltammogram of Pt/Pd (synthesized by Cu deposition) almost overlaps with that of standard Pt. These observations suggest that Pt-deposition is not happening on Pd (without hydrogen) surface by the galvanic displacement of Pd by Pt. This may be due to the negligible difference in their redox potentials (PdCl 2 4 /Pd (0.591 vs. reversible hydrogen electrode (RHE)) and PtCl 2 4 /Pt (0.775 vs. RHE)). The surface hydrogen atoms or Cu atoms on Pd-H and Pd-Cu, respectively, play an important role in reducing Pt 2+ ions and in depositing Pt on Pd. Fig. S1 Cyclic voltammograms (CVs) of Pd (without hydrogen), Pt/Pd (without hydrogen), and Pt/Pd (synthesized by Cu deposition) catalysts recorded in argon-saturated 0.1 M HClO 4 solution at a scan rate of 20 mv s 1. 2

Fig. S2 Oxygen reduction voltammograms of Pd (without hydrogen), Pt/Pd (without hydrogen), and Pt/Pd (synthesized by Cu deposition) catalysts recorded in oxygen-saturated 0.1 M HClO 4 with 1600 rpm at a scan rate of 20 mv s 1. 3

Fig. S3 TEM images of (a) Pt/Pd and (b) Pt/Pd 3 Co. Inset to Figs. S3a and S3b shows EDS line scan of Pt/Pd (Pd (red) and Pt (cyan)) and Pt/Pd 3 Co (Pd (red), Pt (green), and Co (blue)), respectively. 4

Fig. S4 Cyclic voltammograms of Pd and Pd 3 Co catalysts after 100 cycles recorded in argonsaturated 0.1 M HClO 4 solution at a scan rate of 20 mv s 1. 5

Fig. S5 Cyclic voltammograms of (a) Pt/Pd and (b) Pt/Pd 3 Co (initial and after 500 cycles) recorded in argon-saturated 0.1 M HClO 4 solution. Insets to Fig. S5a and S5b show the ORR voltammograms of Pt/Pd and Pt/Pd 3 Co catalysts, respectively. 6

Fig. S6 Cu stripping voltammograms of Pt, Pd, Pt/Pd, Pd 3 Co, and Pt/Pd 3 Co recorded in argonsaturated 12 mm CuSO 4 solution (0.1 M HClO 4 as a supporting electrolyte) at a scan rate of 10 mv s 1. The dotted black and red lines represent the peak positions of Pd and Pt, respectively. 7

Table S1 Inter-planar spacing (d 111 ) of Pd, Pd 3 Co, Pt/Pd, and Pt/Pd 3 Co catalysts calculated from the X-ray diffraction (XRD) patterns. Catalyst Pd Pd 3 Co Pt/Pd Pt/Pd 3 Co d 111 (nm) 0.2257 0.2280 0.2255 0.2274 Table S2 Particle size of Pd, Pd 3 Co, Pt/Pd, and Pt/Pd 3 Co catalysts estimated from the {220} reflection of the X-ray diffraction pattern and from TEM. Catalyst XRD (nm) TEM (nm) Pd Pd 3 Co Pt/Pd Pt/Pd 3 Co 5 3 5 3 ~5 ~3 ~5 ~3 Table S3a EDS analysis of Pt/Pd 3 Co catalyst. Element Atomic % Co 22 Pd 67 Pt 11 Table S3b EDS analysis of Pt/Pd catalyst. Element Atomic % Pd Pt 86 14 8

Table S4 Dispersion of Pd estimated using hard sphere model for different particle sizes. Particle size Total atoms Surface atoms Dispersion (%) (nm) 2.3 440 284 64 3 965 478 49 4 2287 852 37 5.25 5173 1468 28 6 7722 1916 24 10 35751 5324 15 15 120662 11988 10 20 286014 21312 7.5 Calculation of Pt:Pd ratio from dispersion (Table S4) and H des charge For Pd 3 Co Pd 3 Co loading on 0.196 cm 2 of the disk electrode = 3 µg (or 15 µg cm 2 of 20 wt% Pd 3 Co/C) Pd loading on the disk electrode =2.53 µg (Pd:Co is 3:1 molar ratio) The moles of Pd atoms in 2.53 µg of the catalyst = 2.53 10 6 g 106.42 g/mole = 2.37 10 8 mole The total number of Pd atoms = 2.37 10 8 (mole) 6.023 10 23 (atoms/mole) = 14.2 10 15 Dispersion using hard sphere model with 3 nm particle size = 0.49 The total number of surface Pd atoms with 3 nm particle size = 14.2 10 15 0.49 = 6.95 10 15 So, the Pd (surface) : Pd (bulk) = 6.95 10 15 : 14.2 10 15 = 1:2.04 1:2.04 (Pt:Pd) is maximum ratio possible (with Pd 3 Co) if all the surface Pd atoms are metallic with 3 nm particle size. This assumes Pt is deposited on all Pd surface atoms. Thus, 1:4.08 is Pt:Pd ratio possible for half-a-monolayer coverage of Pt on Pd (with Pd 3 Co). H des charge (after correcting for double layer and bulk hydrogen evolution) = 0.650 mc Number of active Pd sites on Pd 3 Co/C = 0.650 mc/1.6 10 19 = 4.06 10 15 Pd atoms 9

(electronic charge in Coulomb =1.6 10 19 C) From the H upd charge the number of surface Pd atoms = 4.06 10 15 Pd atoms. Number of Pt 2+ that can be reduced with Pd-H (surface) = (4.06 10 15 /2) atoms = 2.03 10 15 (since two Pd-H is required to reduce one Pt 2+ ). So, the ratio of Pt:Pd with Pd 3 Co = (2.03 10 15 )/(14.2 10 15 ) = ~ 1:6.99 The above ratio is close to the composition obtained from EDS, ICP, and EDS line scan ~1:6 (in Pd 3 Co). But, we get 1:4.08 from geometric considerations (hard sphere model), since it considers all Pd as metallic. But, only 65% of the surface Pd is metallic (from XPS), and if we correct theoretical value (1:4.06) calculated from geometric considerations (with 0.65) (i.e., 1 0.65:4.08 = 1:6.27). This is almost close to Pt:Pd obtained from H des (1:6.99). For Pd The atomic weight of Pd =106.42 g/mole. The moles of Pd atoms in 3 µg of the catalyst = 3 10 6 g 106.42 g/mole = 2.81 10 8 mole The total number of Pd atoms 2.81 10 8 mole 6.023 10 23 = 16.92 10 15 Dispersion using hard sphere model with 4 nm particle size = 0.37 Number of surface atoms for a 4 nm particle = 16.92 10 15 0.37 = 6.26 10 15 So, the Pd (surface) : Pd (bulk) = 6.26 10 15 :16.92 10 15 = 1:2.70 1:2.70 (Pt:Pd) is the maximum ratio possible (with Pd) if all the surface Pd atoms are metallic with 4 nm particle size. This assumes Pt is deposited on all Pd surface atoms. Thus, 1:5.40 is Pt:Pd ratio possible for half-a-monolayer coverage of Pt on Pd (with Pd). H des charge (after correcting for double layer and bulk hydrogen evolution) = 0.310 mc Number of active Pd sites on Pd = 0.310 mc/1.6 10 19 (electronic charge in Coulomb) 10

= 1.937 10 15 Pd atoms Number of Pt 2+ that can be reduced with Pd-H (surface) = (1.937 10 15 /2) atoms (since two Pd- H is required to reduce one Pt 2+ ) = 0.968 10 15. So, the ratio of Pt:Pd with Pd = (0.968 10 15 )/(16.92 10 15 ) = ~1:17.47 Pt:Pd ratio of 1:17.47 obtained from H upd charge is significantly lower than the experimental composition (1:7 obtained from EDS, ICP, and EDS line scan). In Pd case, the Pt:Pd ratio calculated from the geometric considerations (hard sphere model) is 1:5.40, since it considers all Pd as metallic. Thus, the number of active Pd surface atoms estimated from the H des charge is an underestimation because Pd is oxidizing in the H upd region itself. If we presume ~50 % Pd is oxidizing in the H upd region itself (Pd 3 Co:Pd ESA ratio is 2:1), and if we correct Pt:Pd ratio obtained from H des for this, (i.e., 1/0.5:17.47), then the Pt:Pd ratio is 1:8.73. But, only 65% of the surface Pd is metallic (from XPS), and if we correct theoretical value (1:5.40) calculated from geometric considerations (with 0.65) (i.e., 1 0.65:5.40 = 1:8.30). This is almost close to Pt:Pd ratio obtained from H des (1:8.73). 11

Table S5a Summary of the fitting results for the Pd 3d XPS spectra of Pt/Pd and Pt/Pd 3 Co. Sample Species Binding Energy (ev) Relative Intensity (%) Pt/Pd Pd 0 (metallic) Pd 2+ (PdO) 335.31 336.20 66 34 Pt/Pd 3 Co Pd 0 (metallic) Pd 2+ (PdO) 335.24 335.92 64 36 Table S5b Summary of the fitting results for the Pt 4f XPS spectra of Pt/Pd and Pt/Pd 3 Co. Sample Species Binding Energy (ev) Relative Intensity (%) Pt/Pd Pt 0 (metallic) Pt 2+ (PtO) Pt 4+ (PtO 2 ) 71.25 72.47 74.01 65 21 14 Pt/Pd 3 Co Pt 0 (metallic) Pt 2+ (PtO) Pt 4+ (PtO 2 ) 71.29 72.30 73.75 63 22 15 12