Enhanced Performance of Sn@Pt Core-Shell Nanocatalysts Supported on Two Different Carbon Structures for the Hydrogen Oxidation Reaction in Acid Media

Sustentabilidad de Los Recursos Naturales y Enerǵıa, Cinvestav Unidad Saltillo, Av. Industria Metalúrgica 1062, Parque Industrial Saltillo-Ramos Arizpe, C. P., 25900 Ramos Arizpe, Coah, Mexico Laboratoire des Sciences pour l’Environnement et l’Énergie (LS2E), École Normale Supérieure, Port-au-Prince, Haiti CONACyT, Centro de Investigación Cient́ıca de Yucatán, Km. 5.5 Carr. Sierra Papacal-Chuburná Puerto, Tablaje 31257, Sierra Papacal, Yucatán 97302, Mexico Rathinam Research Center, Rathinam Technical Campus, Coimbatore 641021, Tamilnadu, India Facultad de Ciencias Quı́micas, Universidad Autónoma de Coahuila, C. P., 25280 Saltillo, Coahuila, Mexico CONACyT, Sustentabilidad de los Recursos Naturales y Enerǵıa, Cinvestav Unidad Saltillo, Ramos Arizpe, Mexico


Introduction
PEMFC have reached important niche energy markets over the past years, such as the automotive industry, stationary power applications, and the so-called poly-generation systems [1,2]. PEMFC have relevant advantages over conventional systems based on fossil fuels, including the fact that the use of hydrogen (H 2 ) as the fuel leads to green electrochemical conversion devices [3], in addition to higher energy conversion e ciencies, and zero or very low greenhouse gases (GHG) emissions [1]. Moreover, the concept of green H 2 has gained a great deal of attention recently [4,5]. On this matter, the feasibility of taking advantage of green H 2 produced by low-temperature electrolyzers using it in PEMFC is highly relevant, because of the prospective of reaching a carbon-neutral international energy scenario.
Despite these advantages, it is acknowledged that the cost of PEMFC systems must be reduced, aiming to be more successful in reaching broader markets [2,6]. Some breakdown studies indicate that catalysts may account for 41% of the total cost of a fuel cell stack on the basis of 500,000 units produced per year [7]. us, strategies to reduce the amount of Pt-group metal (PGM) catalysts in PEMFC have been implemented.
Among those approaches, the development of alloyed, metal-metal oxide, and core-shell Pt-based nanocatalysts have demonstrated their effectiveness in reducing the amount of this noble metal, maintaining a high catalytic activity for the hydrogen oxidation reaction (HOR) and oxygen reduction reactions (ORR) at the anode and cathode of PEMFC, respectively. Core-shell nanostructures have unique properties, which are of interest for highperformance PEMFC: (i) the modification of the electronic structure of Pt by the core material, which in turn increases the catalytic activity of the nanostructures by changing the adsorption energy of species; (ii) improved electrochemical stability; and (iii) high Pt utilization because of its exposure to active species being the outermost layer [8,9].
To the best of our knowledge, the assessment of catalytic activity of Pt-based core-shell nanocatalysts for the HOR in acid media is scarce. Wang et al., report the high performance of Ru@Pt core-shell nanocatalysts with ultra-low Pt content for the HOR in acid media, having a 1 : 1 Ru : Pt atomic ratio [13]. Adzic et al. demonstrate a 2-fold enhancement in catalytic activity for the HOR of Ru@Pt coreshell nanoparticles, compared to Pt-Ru alloys. In that study, the Ru@Pt core-shell having a Pt shell thickness of two monolayers shows an increase in specific activity of the HOR by a factor of 1, compared to monometallic Pt [14].
Elsewhere, several Pt-based core-shell nanostructures having Ru, Rh, or Au as the core have shown a high performance for the HOR, however in alkaline media [15][16][17][18]. Nevertheless, the advantages of using supported metal@Pt core-shell nanostructures with a lower Pt content compared to monometallic Pt/C, yet sustaining high performance, encourages the research on those nanocatalysts for the HOR in acid media. On this matter, Sn is an element widely used as cocatalyst of Pt for fuel cell reactions. Because of its higher oxophilicity compared to Pt (0.4 vs. 0.1, respectively) [19], it forms adsorbed OH-species at more negative potentials, transferring them to Pt-sites, facilitating the electrochemical reaction taking place at the noble metal (bifunctional mechanism) [20].
Sn is also significantly cheaper than Pt [21], which results in lower cost Sn@Pt nanocatalysts, also compared to Pt/C. One of the most widely studied applications of Sn as cocatalysts is that for the ethanol oxidation reaction (EOR) at Pt-Sn/C alloys, improving the performance of monometallic Pt/C nanocatalysts through the already mentioned bifunctional mechanism and the electronic effect [22,23]. Sn has been successfully used in the synthesis of intermetallic, random-alloy, and core-shell Pt-based nanocatalysts [24,25].
Precisely, one of the most effective methods of synthesis of noble metal nanocatalysts is the bromide anion exchange (BAE) process. Early reports highlight the advantages of implementing this surfactant-free method, which include the following: (i) avoiding the presence of organic molecules that may prevent the adsorption of active species at the metal sites of the nanocatalysts; (ii) controlling the particle size growth, enhancing the electrochemically active surface area (ECSA); and (iii) being a suitable and straightforward, environmentally friendly method [26][27][28].
In this work, Sn@Pt/C and Sn@Pt/NG nanocatalysts (where C: commercial Vulcan XC-72 and NG: homesynthesized N-doped graphene) have been synthesized by the BAE method. eir catalytic activity for the HOR is characterized by acid electrolyte and compared to that of monometallic Pt/C and Pt/NG.

Experimental
2.1. Heat Treatment of Vulcan XC-72 and Synthesis of Nitrogen-Doped Graphene (NG). Vulcan powders were heat treated at 400°C for 4 h in N 2 atmosphere, aiming to eliminate surface impurities [29]. NG was obtained by mixing graphite flakes and urea in a 10 : 90 wt. ratio. e mixture was submitted to ball milling using a Restch PM 200 apparatus in a balls: material weight ratio of 5 : 1, at 300 rpm for 8 h, pausing for 30 min after every hour of milling. e resulting material was passivated in N 2 for 12 h, followed by pyrolysis at 500°C in N 2 atmosphere for 1 h.

Synthesis of Core-Shell Nanocatalysts by the Bromide Anion Exchange (BAE) Method.
KBr and NaBH 4 were used as solvents and reducing agents, respectively, [30]. Nominally, a metal: carbon weight ratio of 20 : 80 was expected for the core-shell nanostructures, with a theoretical Pt : Sn atomic ratio of 1 : 1. As an example, for the synthesis of Sn@ Pt/C, in the first step Sn/C was synthesized as follows: 21.57 mg of SnCl 6 ·2H 2 O were stirred in 95.6 mL deionized water for 5 min, followed by the addition of 16.6 mg of KBr maintaining agitation for 10 min (n KBr /n metallic salt ratio � 1.46). A solution containing 120 mg of C was adjusted to the mixture, which was submitted to ultrasound for 45 min. Afterward, 14.3 mL of a 0.1 M NaBH 4 solution was added (n NaBH4 /n metallic salt ratio � 15), applying magnetic stirring at 40°C for 2 h. e obtained powders were filtered, washed with deionized water, and dried at 50°C for 12 h.
In a second step, the Pt shell was deposited on the core material by stirring 48.2 mg of H 2 PtCl 6 ·6H 2 O in 92.9 mL of deionized water for 5 min, with the subsequent addition of 16.15 mg of KBr keeping agitation for 20 min (n KBr /n metallic salt ratio � 1.46). To this mixture, 128 mg of Sn/C were adjusted, followed by ultrasound agitation for 45 min. en, 13.9 mL of 0.1 M NaBH 4 were added by applying magnetic stirring at 40°C for 2 h (n NaBH4 /n metallic salt ratio � 15). e powders were filtrated, washed with deionized water, and dried at 50°C for 12 h. Sn@Pt/NG, Pt/C, and Pt/NG were obtained following the same procedure.

Physicochemical and Electrochemical Characterization.
Details of the physiochemical and electrochemical characterization were reported previously [31][32][33][34]. Briefly, textural properties of the supports were obtained in a Quantachrome Instruments Autosorb1 analyzer. XRD patterns were acquired in a Bruker D2 Phaser apparatus in the 2θ interval from 10 to 100°. Crystallite size was determined using the following Scherrer equation: where k � 0.9, λ is the wavelength of the X-rays (0.1541 nm), B is the full width at half height of the reflection, and θ is the peak maximum of the reflection. e lattice parameter a fcc was calculated from the following equation: e chemical composition reported is the average of 5 micro areas analyzed by EDS in a Philips XL30 SEM microscope. Characterization by TEM was performed in a Jeol 2100 microscope, operating at 200 kV. XPS analysis was carried out using a ermo Scientific K-Alpha + XPS apparatus (hv � 1486.68 eV).
A three-electrodes setup was used for electrochemical characterization in 0.5 M H 2 SO 4 , using a WaveDriver 20 bipotentiostat equipped with a rotating disc electrode setup (Pine Inst.). e reference electrode was an Ag/AgCl (saturated KCl), while the counter was a Pt coil, both placed in separated chambers from the main electrolyte. e working electrode was a 5 mm diam glassy carbon. Catalyst inks were prepared by dispersing for 30 min in ultrasound 5 μL Nafion ® solution, 1 mL 2-propanol, and 10 mg of nanocatalyst powder. Aliquots of 10 μL were deposited on the glassy carbon. All potentials were reported on the RHE scale.
Cyclic voltammograms (CV) were acquired in the 0.05-1.2 V vs. RHE interval at 20 mV·s −1 in N 2 atmosphere. e electrochemically active surface area (ECSA H ) and the real area (A r ) were determined to take the charge due to the desorption of hydrogen in the hydrogen adsorption/desorption region (H ads/des ) of the CV, according to the following equations: where Q is the experimental electrical charge due to the desorption of hydrogen; Q H is the theoretical charge due to the desorption of one monolayer of hydrogen on Pt (210 μC·cm −2 ); and L Pt is the Pt loading on the electrode. Accelerated degradation tests (ADT) were performed on the nanocatalysts by submitting them to 1000 cycles in the same potential interval indicated above, at a scan rate of 200 mV·s −1 . CO-stripping polarization curves were obtained by bubbling CO for 10 min, while polarizing the working electrode at 0.05 V vs. RHE, then purging it by flowing N 2 in the electrolyte for 20 min. CV was acquired in the same mentioned potential window at 20 mV·s −1 .
e catalytic activity of the nanocatalysts for the HOR was evaluated in a rotating disc setup. H 2 was bubbled in the acid electrolyte for 20 min, after which polarization curves were plotted at rotation rates ω of 400, 800, 1200, 1600, and 2000 rpm, in the 0-0.65 V vs. RHE range. Curves compensated for iR drop were reported in this work. e R value of the 0.5 M H 2 SO 4 was determined from EIS measurements. Koutecky-Levich plots were obtained using the well-known Levich equation as follows: where j d , j k , and j are the diffusion-controlled, kinetic, and measured current density, respectively. e kinetic current i k was obtained with the following equation: where i d and i are the diffusion-controlled and measured current, respectively. From equation (5), mass and specific Tafel plots were obtained by normalizing i k by the Pt mass content and A r , respectively. Figure 1 shows the XRD patterns of the nanocatalysts. Pt/C has reflections ascribed to (002) due to the graphitic zones in the structure of Vulcan, and the (111), (200), (220), (311), and (222) planes of the fcc structure of Pt (PDF 00-004-0802). Sn@Pt/C shows the same peaks, with similar features. Moreover, no noticeable shift in the position of the peaks between the monometallic and the core-shell nanocatalysts has been observed. Such characteristic suggests that no atoms of the Sn core have incorporated into the Pt shell contracting it and provoking the formation of alloyed phases, as has been reported elsewhere for some other core-shell nanostructures [35,36]. Additionally, the broadness of the reflections suggests the nanosized feature of the anode materials. Meanwhile, Pt/NG and Sn@Pt/NG have an intense reflection due to the (002) plane characteristic of graphene-like structures, as well as the (101) and (004) peaks also ascribed to the support [37]. Moreover, both nanocatalysts show the peaks attributed to fcc Pt, also without a noticeable shift in their position. Figure S1 in the supplementary information file shows the XRD patterns of the graphite flakes, NG, and Vulcan. e first two have high-intensity and low-intensity very narrow peaks at 2θ � 26.5 and 54.54°, attributed to the (002) and (004) carbon planes, characteristic of graphitic materials, respectively. ese characteristics support the observations in the previous paragraph of the patterns shown in Figure 1. Vulcan shows broader peaks due to the (002) and (101) reflections of carbon at 2θ � 25 and 44.39°, respectively. e position of the (002) plane in Vulcan correlates well with previous reports in the literature [38]. Overall, graphite and NG show crystalline features, while Vulcan is rather amorphous in nature.

Results and Discussion
Features of the nanocatalysts from Figure 1 are shown in Table 1. e crystallite size (d XRD ) ranges from 3.4 to 6.1 nm, the smallest one being that of Sn@Pt/C, while the nanocatalysts supported on NG have larger values. Interestingly, there is no variation in lattice parameter (a fcc ) when comparing the monometallic nanocatalysts to the core-shell Sn@

Journal of Chemistry
Pt nanostructures on each carbon support, which indicates that the Pt lattice has suffered no contraction. Figure S2 shows the Raman spectra of graphite, NG, and Vulcan. Peaks ascribed to the D, G, and 2D bands are observed at 1350, 1580, and 2670 cm −1 , respectively. e G band originates because of the stretching of sp 2 C-C bonds, and it is related to the structural order of the carbon material [39]. e D and 2D bands emerge from stretching vibrations of hybridized sp 2 and sp 3 bonds, indicating the degree of structural disorder of the samples [39]. us, the ratio of the relative intensities of the D and G bands (I D /I G ) is an indicator of the degree of structural disorder or crystallinity of the materials [40].
Graphite has an I D /I G ratio of 0.04, confirming its highly crystalline structure. NG has the same peaks as graphite. However, the relative intensity of its D band increases considerably, resulting in I D /I G � 0.86. Such a result confirms the structural modification of NG, i.e., an increased disorder suggesting the formation of graphene layers or exfoliated graphite after ball milling. Moreover, the increased disorder observed for NG can be attributed to the doping with heteroatoms [39]. Meanwhile, Vulcan has an I D /I G ratio of 1.49, evidencing its disordered characteristic. Table 2 shows the chemical composition of the nanocatalysts from EDS analysis. e Pt content at Pt/C and Pt/ NG is lower than nominally expected, although the O concentration is higher than 2 wt. %. Moreover, 3.27 wt. % of N has been detected at Pt/NG, which has a C content close to 80 wt. % theoretically expected. On the other hand, the C content at Sn@Pt/C is higher than the nominal one, while Sn@Pt/NG shows 81.81 of this element, along with 5.68 (wt. %) of N. Meanwhile, the Pt : Sn ratio at Sn@Pt/C and Sn@Pt/ NG is higher than theoretically expected.  (Table 1). Figure (B) is an HRTEM micrograph of the core-shell nanocatalyst. FFT analysis allows to characterization of the nanoparticles by generating SAED patterns (inset). Two interplanar distances have been determined: (i) 0.195 nm at the center of the nanoparticle, which has been ascribed to the (211) reflection of Sn [41], even though the (200) peak of Pt may have a somehow similar value [42]; (ii) 0.220 nm at the border of the nanoparticle, attributed to the (111) plane of Pt [43].   (Table 1). Analysis by FFT in (B) also demonstrates two interplanar distances at this nanocatalyst: (i) 0.198 nm at the center ascribed to Sn (211); (ii) 0.216 nm at the border ascribed to Pt (111). Figure (C) is the dark field micrograph of the nanocatalyst. ese features support the core-shell nature of nanostructured Sn@Pt/C and Sn@Pt/NG. Table S1 depicts the surface chemical composition of the nanocatalysts by XPS. Under this perspective, the nanocatalysts have a Pt concentration between 0.68 and 2.97 (at. %). Interestingly, the Pt : Sn at. ratio of Sn@Pt/C and Sn@Pt/ NG reaches a value closer to the nominal than in Table 2, more clearly seen at Sn@Pt/C (1.0 : 0.87). It is noteworthy that by using the XPS technique, no N species have been detected at the nanocatalysts supported on NG. Such difference compared to EDS analysis ( Table 2) has been attributed to the sensitivity of XPS, which is a superficial characterization technique. e high-resolution XPS spectra of Pt/C in the Pt 4f region is shown in Figure 3(a). Two doublets due to the spinorbit splitting into the Pt4f 7/2 and Pt4f 5/2 states are observed. Pt 0 and Pt 2+ species are identified at the nanocatalyst [43], the former having a higher relative concentration (Table S2). Similar doublets can be seen at Pt/NG (Figure 3(b)), also having a higher concentration of Pt 0 compared to Pt 2+ species (Table S2).
Figures 3(c) and 3(d) are the high-resolution spectra in the Pt 4f region of Sn@Pt/C and Sn@Pt/NG, respectively. Both core-shell nanostructures show the two doublets in the Pt4f 7/2 and Pt4f 5/2 states. As in the case of the monometallic nanocatalysts mentioned above, both core-shell nanostructures develop a higher relative concentration of Pt 0 compared to Pt 2+ (Table S2)    been formed at the nanocatalysts. ese results confirm the observations in Figure 1, where no reflections associated with metallic Sn have emerged. Figures S3 and S4 show the spectra of the nanocatalysts in the C 1 s and O 1 s regions, respectively. In particular, the presence of PtO bonds at the nanocatalysts in Figure S4 correlates well with the development of Pt 2+ species in the Pt 4f region in Figure 3. e other bonds are typically observed at carbon-supported Pt nanocatalysts [33]. Figure 4 shows CVs of (a) Pt/C, (b) Pt/NG, (c) Sn@Pt/C, and (d) Sn@Pt/NG before (1 st cycle) and after (1000 th cycle) ADT. Considering the chemical composition reported in Table 2, the total metal loading at the working electrodes is 72.3, 75.9, 51.2, and 39.18 mg cm −2 at Pt/C, Pt/NG, Sn@Pt/C,   and Sn@Pt/NG, respectively. A typical negative variation in j is observed after ADT at three of the nanocatalysts ascribed to agglomeration and segregation of nanoparticles, while Pt/ NG has an increase after cycling over the potential window, which suggests the activation of Pt sites due to the test. As indicated, the electric charge due to desorption within the H ads/des region has been used to determine their A r before ADT, and their ECSA H at the 1 st and 1000 th cycle. Table 3 shows the values of these parameters. Pt/C has the largest A r and ECSA H values before ADT. In fact, its ECSA H is similar to previous reports elsewhere on analogous Pt/C nanocatalysts [23]. Nevertheless, Pt/C has the most important negative variation in ECSA H (-32.7%), of the same order as reported previously [23], and roughly 10 times higher than that of the Sn@Pt/C core-shell nanocatalyst. Pt/NG shows high stability and even gains active surface area after ADT.
Meanwhile, Sn@Pt/NG shows a more important negative variation in ECSA H than Sn@Pt/C. e active surface area has also been determined from CO-stripping tests (ECSA CO ) before ADT, as shown in Figure S5, where the first cycle is the CO oxidation, while the second one indicates the behavior of the clean surface of the nanocatalysts in the N 2 -saturated electrolyte. Table 3 shows the ECSA CO values obtained, which overall are higher than their ECSA H counterparts. e nanocatalyst with the highest ECSA CO value is also Pt/C, while the tendency at the other nanocatalysts resembles that of ECSA H before ADT.  Moreover, the shape of the CO oxidation plots shows the effect of both the chemical composition of the nanocatalysts and the type of support used. Pt/C has a characteristic narrow peak of monometallic Pt nanocatalysts supported on Vulcan [44], with a maximum current density peak due to the oxidation of CO (j CO ) at 0.76 V/RHE and an onset potential (E onset, CO ) of 0.54 V/RHE (Table 3). e use of the NG support has an important effect on Pt/NG by shifting E onset, CO by 0.19 V toward more negative values compared to Pt/C. Additionally, a broad shoulder with two peaks (0.67 and 0.72 V/RHE) is observed at Pt/NG, different than the sharp peak at Pt/C. is behavior of monometallic Pt has been ascribed to arbitrary nucleation of Pt nanoparticles onto sp 2 and sp 3 carbon domains [44].
Interestingly, despite being supported on Vulcan, Sn@ Pt/C also shows a broad shoulder with two peaks, i.e., there is a significant effect of the chemical composition of the nanocatalyst on the oxidation of CO. Such behavior has been attributed elsewhere to two Pt states induced at a Pt shell by a Ru core [45], which is analogous to the effect of Sn on the Pt shell in this work. Moreover, the fact that the two peaks shown by Sn@Pt/C are at more negative potentials (0.67 and 0.72 V/RHE, Table 3) than that of Pt/C, indicates a displacement of the d-band center of the Pt shell due to a compressive strain effect provoked by the Sn core [45]. Additionally, E onset, CO � 0.4 V/RHE at Sn@Pt/C, i.e., more negative than Pt/C, although 50 mV more positive than Pt/ NG.
Meanwhile, Sn@Pt/NG shows peaks at 0.67 and 0.77 V/ RHE, ascribed to an effect of both carbon support and chemical composition of the nanocatalyst, with E onset, CO � 0.4 V/RHE (Table 3). Elsewhere, CO-stripping has been proposed as an electrochemical tool to characterize coreshell nanostructures [46]. e shape of the CO-stripping curves of Sn@Pt/C and Sn@Pt/NG in Figure S5 differs completely from those of Pt-Sn/C alloyed nanocatalysts in [23], which provides more evidence that effectively coreshell nanostructures have been obtained following the synthesis procedure proposed in this work. e iR-compensated mass polarization curves of the HOR at (a) Pt/C, (b) Pt/NG, (c) Sn@Pt/C, and (d) Sn@Pt/ NG are shown in Figure 5. It should be mentioned that an R value of about 6 W has been determined for the electrolyte, in good agreement with the literature [47,48]. A compensation of 80% of the electrolyte resistance has been considered in the plots [49]. As can be observed, at 0.4 V/ RHE and 1600 rpm, the mass limiting current density (j l, m ) is significantly higher at Sn@Pt/C and Sn@Pt/NG with an almost 2-fold increase compared to Pt/C and even larger related to Pt/NG (Table 4), demonstrating an important  Journal of Chemistry positive effect of applying the core-shell nanostructures to promote the HOR. e j l, m value is about the same for the two core-shell nanostructures, suggesting a dominant promotion of the reaction by the Sn@Pt nanoparticles, rather that the use of the NG support. Furthermore, the specific activity of the nanocatalysts for the HOR is shown in Figure S6. e specific limiting current density (j l, s ) is clearly higher at Sn@Pt/C and Sn@Pt/NG, compared to Pt/C (which has the lowest performance) and Pt/NG (Table 4). In fact, Sn@Pt/C shows an almost 7 and 3fold increase in j l, s related to Pt/C and Pt/NG, respectively. Moreover, Sn@Pt/C demonstrates a higher geometric catalytic activity than the other nanocatalysts, as seen in Figure S7 and Table 4. us, based on the mass, specific, and geometric data in Table 4, Sn@Pt/C has the highest catalytic activity for the HOR, followed by Sn@Pt/NG. Figure 6 shows the Koutecky-Levich plots of the HOR at Sn@Pt/C and Sn@Pt/NG, obtained from Equation (4). A theoretical Koutecky-Levich plot of a mechanism of the HOR involving a 2 e − transfer has been obtained with the following equation [50,51]: where the Koutecky-Levich slope is 1/B, while n: number of electrons transferred (n � 2); F: Faraday constant (96, 500°C); ]: kinematic viscosity (0.01 cm 2 ·s −1 ); D: hydrogen diffusion  Journal of Chemistry coefficient (3.7 × 10 −5 cm 2 ·s −1 ); and C H2 : concentration of H 2 in H 2 SO 4 (7.14 × 10 −7 mol·cm −3 ) [38]. As can be seen in Figure 6, the experimental slopes approach the theoretical one, strongly suggesting that the HOR at the core-shell nanocatalysts undergo a mechanism involving a 2 e − transfer, in good agreement with the HOR reaction in acid media as follows: Tafel plots of mass and specific activity of the nanocatalysts for the HOR are shown in Figures 7(a) and 7(b), respectively. In both scenarios, the catalytic activity decreases in the order Sn@Pt/C > Sn@Pt/NG > monometallics.
us, there is a significant promotion effect of the core-shell nanostructures for the reaction, which is ascribed to an electronic effect (modification of the Pt d-band center due to interactions of the shells with the Sn cores). e bifunctional mechanism, due to the oxophilicity of Sn, may have also contributed to the high performance of the core-shell nanocatalysts. Table 5 shows a comparison of catalytic activity of Sn@ Pt/C with that of some nanocatalysts reported in the literature in acid media. It should be mentioned that most of the data are rough values determined from the plots reported at each work. When considering j L, geo (which is the most widely reported), Sn@Pt/C performs very well, with a value of 2.55 mA·cm −2 , which is slightly higher than that reported for a TKK 46% Pt/C nanocatalyst [52]. In some cases, polycrystalline Pt [53,54], RuO 2 -Pt/C [55], and PtMo-CeOx-NAs [56] show a higher j L, geo . Meanwhile, the value reported for a Pt-PdO/C nanocatalyst is similar to that of Sn@Pt/C [57].
Attention should be paid, however, to the mass and specific activities for the HOR. e i m and i s values of Sn@Pt/ C are roughly one-third and one-half of those reported by Cui et al. for their PtMo-CeOx-NAs nanocatalyst, respectively, [56]. Meanwhile, the i m of Sn@Pt/C is higher than that of the Pt-PdO/C nanocatalyst reported by Barman et al., even though the authors report the mass activity by total metal loading [57]. us, further studies should focus on increasing the mass and specific activities of Sn@Pt/C.

Conclusions
e BAE method produced nanostructured catalysts. Physicochemical and electrochemical characterizations showed the formation of Sn@Pt/C and Sn@Pt/NG core-shell nanocatalysts. From XPS analysis, Pt 0 and Pt 2+ species were detected at all nanocatalysts, while only Sn 2+ formed at Sn@ Pt/C and Sn@Pt/NG. CO-stripping tests provided evidence of a displacement of the Pt d-band center of the Pt shells because of a strain effect attributed to the Sn cores. Such electronic modification, as well as the bifunctional mechanism due to the oxophilicity of Sn, contributed to the higher mass and specific catalytic activity of the core-shell nanocatalysts for the HOR, particularly Sn@Pt/C. Both Sn@Pt/C and Sn@Pt/NG promoted the HOR via a 2 e − transfer mechanism.
Data Availability e data used to support this study are included within the supplementary information files.

Conflicts of Interest
e authors declare that they have no conflicts of interest.

Supplementary Materials
Figures S1 and S2 show the XRD patterns and the Raman spectra of graphite, NG, and Vulcan, respectively. Table S1 depicts the chemical composition of the nanocatalysts as determined by XPS. Table S2 shows the parameters of the nanocatalysts, obtained from XPS analysis. Figures S3 and S4 show the high-resolution spectra in the C 1 s and O 1 s regions of the nanocatalysts, respectively. Figure S5 depicts the CVs resulting from the CO-stripping test at the nanocatalysts. Figure S6 shows the polarization curves of the HER (specific activity) at the nanocatalysts. Figure S7 shows the polarization curves of the HER (geometric activity) at the nanocatalysts. (Supplementary Materials) Journal of Chemistry 9