Evaluation of the Scaffolding Effect of Pt Nanowires Supported on Reduced Graphene Oxide in PEMFC Electrodes

: The stacking and overlapping effect of two-dimensional (2D) graphene nanosheets in the catalyst coating layer is a big challenge for their practical application in proton exchange membrane fuel cells (PEMFCs). These effects hinder the effective transfer of reactant gases to reach the active catalytic sites on catalysts supported on the graphene surface and the removal of the produced water, ﬁnally leading to large mass transfer resistances in practical electrodes and poor power performance. In this work, we evaluate the catalytic power performance of aligned Pt nanowires grown on reduced graphene oxide (rGO) (PtNW/rGO) as cathodes in 16-cm 2 single PEMFCs. The results are compared to Pt nanoparticles deposited on rGO (Pt/rGO) and commercial Pt/C nanoparticle catalysts. It is found that the scaffolding effect from the aligned Pt nanowire structure reduces the mass transfer resistance in rGO-based catalyst electrodes, and a nearly double power performance is achieved as compared with the Pt/rGO electrodes. However, although a higher mass activity was observed for PtNW/rGO in membrane electrode assembly (MEA) measurement, the power performance obtained at a large current density region is still lower than the Pt/C in PEMFCs because of the stacking effect of rGO.


Introduction
With the commercial release of the Toyota Mirai and Hyundai ix35 fuel cell vehicles, the viability of using proton-exchange membrane fuel cells (PEMFCs) as the power source in transport applications has been demonstrated.However, for the widespread adoption of such vehicles, larger power outputs and long-term durability are required at a reduced cost [1,2].Due to the sluggish oxygen reduction reaction (ORR) at the cathode in PEMFCs, catalysis is required.Platinum group metals (PGM), and specifically platinum (Pt), are inherently the most active catalysts towards the ORR [3] as well as the most stable in the acidic conditions of the PEMFC.However, due to their high cost and low performance compared to theoretical values, much effort has been directed to developing novel methods of reducing the PGM content while increasing the catalytic activity [4].
One-dimensional (1D) Pt nanostructures such as nanowires and nanotubes have received increasing interest in recent years [5].Sun et al. synthesized Pt nanowires supported on carbon black (PtNW/C) by the simple wet chemical route of using formic acid to reduce chloroplatinic acid to Pt metal [6].This catalyst demonstrated enhanced ORR activities as the favored Pt growth along the (111) crystallographic plane promoted by the slow reduction rate, and the regular arrays improved the intrinsic catalytic activity and mass transport limitations, respectively.This theory has been supported by Du's group, in whose work the synthesis conditions were optimized for the in situ growth of PtNWs directly on carbon paper gas diffusion layers (GDLs) [7,8].
To help maximize catalyst utilization ratio in PEMFC electrodes as well as improve stability, PGM catalysts are commonly supported on carbon blacks [9].High surface area carbon blacks such as the Vulcan XC-72R are typically used due to the large catalyst electrochemically active surface areas (ECSA) obtainable from the provided porous network.However, a caveat of the porous network is the fact that many PGM catalyst particles can become trapped inside nanopores, where electrolyte ionomer cannot access them to form effective active sites.Carbon blacks also suffer from carbon corrosion due to the relatively low oxidation potential of carbon [10].In an attempt to address these issues as well as in order to minimize charge transfer resistances in the catalyst layer, various carbonaceous supports such as carbon nanotubes (CNTs), carbon nanofibers (CNFs) and graphene have been investigated [11][12][13].Of particular interest is the reduced graphene oxide (rGO), wherein the impurities from incomplete reduction provide much needed nucleation sites on the otherwise pristine graphene sheets.These functional groups have also been shown to help improve the carbon monoxide poisoning tolerance of the impurity in fuel cell gases as well as enhance reaction activities [14][15][16].
In combining the two areas of interest, PtNWs have been grown on rGO supports [14] as well as sulfur-doped graphene (SG) [17].Although the latter referenced work showed an even distribution of nanowires on the rGO supports, branched nanowires formed to the anchoring oxygen functional groups.To help address this issue, Du et al. [15] introduced palladium (Pd) nanoseeds onto PVP-functionalized rGO sheets to grow uniform PtNWs.With improved distribution on the entire rGO surface, uniform nanowires were demonstrated to lead to enhanced catalytic activity.
However, the two-dimensional (2D) nature of the graphene-based catalysts makes them very difficult to use in practical electrodes in PEMFCs.In the drying process of the catalyst layer made by coating rGO-based catalyst inks, the rGO nanosheets stack on top of each other to form a dense catalyst layer, exacerbating the mass transfer limitations for both the reactant fuel and the produced water diffusing through the layer [16,18].Considering the encouraging ORR catalytic activities of PtNWs/rGO, the intention of this work is to evaluate the scaffolding effect of the unique PtNWs/rGO structure by in situ testing in single PEMFCs.Fuel cells with cathodes from Pt nanoparticles supported on rGO (Pt/rGO) and commercial Pt/C nanoparticle catalysts are also fabricated as benchmarks to help understand the stacking effect of rGO nanosheets and the enhanced scaffolding effect from the nanowire geometry.

Preparation of PVP-Functionalized rGO
Two and a half milliliters of the 2 wt % GO suspension were diluted with 197.5 mL of H 2 O.The resulting dispersion was sonicated with a 130 W, 20 kHz sonic horn at 40% amplitude for 30 min.Then 800 mg of PVP were added and the mixture was stirred for 12 h.Next 200 mg of L-Ascorbic acid were added to the mixture, which was subsequently heated to 95 • C. The mixture was then stirred for 1 h before centrifugation once with H 2 O.The rGO was then dispersed in H 2 O to provide a 25 mL suspension.Two and a half milliliters of the as-prepared rGO suspension were diluted with 17.5 mL of H 2 O. Two separate suspensions were prepared.

Preparation of Pt/rGO
The preparation of Pt/rGO followed the process reported [19].Two milliliters of the H 2 PtCl 6 solution were added to one of the diluted rGO suspensions.Separately, 62 mg of NaBH 4 were dissolved in 20 mL of H 2 O, which was added dropwise to the reaction mixture under sonication by a sonic bath.After 1 h of sonication time, the reaction mixture was left to settle overnight before being washed and collected by centrifugation in H 2 O twice, followed by once with IPA.The catalyst was dispersed in IPA to provide a suspension of concentration 5 mg Pt mL −1 .

Preparation of Pt(NW)Pd/rGO
Pt(NW)Pd/rGO was prepared following the procedure previously reported by our group [15].Typically, 53.3 µL of the stock PdCl 2 solution was added to one of the diluted suspensions of rGO.Then 0.8 mL of HCOOH was added and the mixture was left to stir at room temperature for 16 h.Afterwards, a further 40 mL of H 2 O were added, followed by 2 mL of the H 2 PtCl 6 solution.Next 6.64 mL of HCOOH were added and the reaction mixture was left to react for 72 h.Centrifugation and dispersion of this catalyst in IPA followed the same procedure detailed for Pt/rGO.

Membrane Electrode Assembly (MEA) Preparation and Physical Characterization
To obtain suitable catalyst loadings of 0.4 and 0.6 mg Pt cm −2 within electrodes, sufficient quantities of commercial Pt/C, Pt/rGO and Pt(NW)Pd/rGO suspensions were added to separate sample vials and 113 µL of 10 wt % Nafion solution were added to each.In the case of Pt/C, 0.875 mL of IPA was added to disperse the catalyst black.The catalyst inks were sonicated by a 130 W, 20 kHz sonication horn for 10 min at 20% power.The gas diffusion electrodes (GDEs) were made by coating the catalyst inks through painting onto 16 cm 2 Sigracet 35 BC carbon paper gas diffusion layers (GDLs).After leaving them to dry at room temperature, the electrodes were hot-pressed to a 36 cm 2 piece of Nafion ® 212 membrane at 1800 lb load for 2 min at 135 • C with commercial JM Pt/C anodes with a catalyst loading 0.4 mg Pt cm −2 .The GDE surface was imaged using a Philips (Amsterdam, The Netherlands) XL-30 FEG Environmental SEM operating at 20 kV.

Single Cell Testing
The MEAs were tested in a PEM fuel cell stand (FCT-50S, PaxiTech-BioLogic, Grenoble, France) with electrochemical impedance spectroscopy (EIS) capabilities.A polytetrafluoroethylene (PTFE) gasket of thickness 254 µm was used at both the cathode and anode sides.The membrane was hydrated by holding the cell potential at 0.6 V for 14 h at the cell temperature of 80 • C. The reactant gases were fully humidified H 2 /air at the anode and cathode, respectively, with a backpressure of 0.5/0.5 bar and stoichiometry of 1.3:2.4,respectively.To measure the electrochemically effective surface area (ECSA) of the catalysts in the electrodes, the cathode gas was then switched to N 2 .After 30 min, 200 cycles of cyclic voltammetry (CV) scan were conducted to the cathodes between 0.05 and 1.2 V at a sweep rate of 50 mV s −1 , followed by three scans at 20 mV s −1 .The third scan at 20 mV s −1 was used for the ECSA calculation.The cell potential was then held at 0.5 V for 30 min and the average current obtained was used for H 2 crossover correction in the mass activity measurement in the MEA.The reactant gas at the cathode was then changed back to air and, after being held stable for 30 min, the cell polarization curve was recorded at 1 mV s −1 between the open circuit voltage (OCV) and ca.0.3 V. Electrochemical impedance spectroscopy (EIS) analysis was run at 0.65 V in the frequency range 10 kHz-0.1 Hz with an amplitude of 10 mV.To measure the mass activity of the catalyst in the electrode, the cathode was then switched to O 2 gas and a polarization curve was recorded at 1 mV s −1 with fully humidified H 2 /O 2 at stoichiometry of 2/9.5, respectively.

SEM Analysis of GDEs
Figure 1 shows the surface SEM images of the GDEs made from Pt/C, Pt/rGO, and Pt(NW)Pd/rGO.The GDE with Pt/C nanoparticle catalysts displays many large cracks (Figure 1a) with a land size of several hundred micrometers, which is in agreement with our former research; these cracks are considered essential for gas diffusion through the whole catalyst layer, together with the mesoporous network formed by the high surface area carbon support (Figure 1b) [20].When rGO is introduced, as shown in Figure 1c,e, the number of cracks significantly decreases.Both GDEs from Pt/rGO and Pt(NW)Pd/rGO exhibit a very similar structure.This change can be ascribed to the stacking of the rGO within the catalyst layer and the 2D rGO nanosheets overlapping with each other to form a much denser coating layer.Comparing with the one from Pt/C nanoparticles shown in Figure 1a, this dense structure provides much less of a path for the gas diffusion through the catalyst layer, and thus a larger mass transfer resistance and a lower power performance is expected in the operation of PEMFCs.Figure 1d,f also show very few large aggregates on the electrode surface, demonstrating the good distribution of the rGO-based catalysts within the catalyst layer.

SEM Analysis of GDEs
Figure 1 shows the surface SEM images of the GDEs made from Pt/C, Pt/rGO, and Pt(NW)Pd/rGO.The GDE with Pt/C nanoparticle catalysts displays many large cracks (Figure 1a) with a land size of several hundred micrometers, which is in agreement with our former research; these cracks are considered essential for gas diffusion through the whole catalyst layer, together with the mesoporous network formed by the high surface area carbon support (Figure 1b) [20].When rGO is introduced, as shown in Figure 1c and 1e, the number of cracks significantly decreases.Both GDEs from Pt/rGO and Pt(NW)Pd/rGO exhibit a very similar structure.This change can be ascribed to the stacking of the rGO within the catalyst layer and the 2D rGO nanosheets overlapping with each other to form a much denser coating layer.Comparing with the one from Pt/C nanoparticles shown in Figure 1a, this dense structure provides much less of a path for the gas diffusion through the catalyst layer, and thus a larger mass transfer resistance and a lower power performance is expected in the operation of PEMFCs.Figures 1d and 1f also show very few large aggregates on the electrode surface, demonstrating the good distribution of the rGO-based catalysts within the catalyst layer.

In Situ Testing
The GDEs were tested in H2/air PEMFCs and the polarization and power density curves are shown in Figure 2. Pt(NW)Pd/rGO shows a much higher power performance than Pt/rGO.At 0.6 V,

In Situ Testing
The GDEs were tested in H 2 /air PEMFCs and the polarization and power density curves are shown in Figure 2. Pt(NW)Pd/rGO shows a much higher power performance than Pt/rGO.At 0.6 V, the conventional operation voltage for PEMFCs in practical applications, the power densities for the Pt(NW)Pd/rGO and Pt/rGO electrodes are 0.206 and 0.128 W cm −2 , respectively, at a catalyst loading of 0.4 mg Pt cm −2 .The high power density of the Pt(NW)Pd/rGO electrode demonstrates the positive scaffolding effect from using nanowires.When increasing the catalyst loading from 0.4 to 0.6 mg Pt cm −2 , the power performance for the Pt(NW)Pd/rGO and Pt/rGO electrodes increases very little-by only 9.7% or 3.1% to 0.226 or 0.132 W cm −2 , respectively-indicating the mass transfer limitations within the practical rGO-based electrodes, as mentioned by Antolini [16].The increase of catalytic activities of the catalysts within the electrodes cannot really convert to the improvement of electrode power performance in PEMFC devices.The enhancement observed for nanowire electrodes even leads to high power density over the Pt/C nanoparticle electrode at a low current density range below 0.1 A cm −2 .However, the power performance is still much lower as compared with the Pt/C nanoparticle electrode at the large current density region, where a power density of 0.314 W cm −2 is achieved at 0.6 V.The poor power performance with rGO-based electrodes is in line with the dense electrode structure shown in the SEM analysis in Figure 1.
Coatings 2018, 8, x FOR PEER REVIEW 5 of 9 Pt(NW)Pd/rGO and Pt/rGO electrodes are 0.206 and 0.128 W cm −2 , respectively, at a catalyst loading of 0.4 mgPt cm −2 .The high power density of the Pt(NW)Pd/rGO electrode demonstrates the positive scaffolding effect from using nanowires.When increasing the catalyst loading from 0.4 to 0.6 mgPt cm −2 , the power performance for the Pt(NW)Pd/rGO and Pt/rGO electrodes increases very little-by only 9.7% or 3.1% to 0.226 or 0.132 W cm −2 , respectively-indicating the mass transfer limitations within the practical rGO-based electrodes, as mentioned by Antolini [16].The increase of catalytic activities of the catalysts within the electrodes cannot really convert to the improvement of electrode power performance in PEMFC devices.The enhancement observed for nanowire electrodes even leads to high power density over the Pt/C nanoparticle electrode at a low current density range below 0.1 A cm −2 .However, the power performance is still much lower as compared with the Pt/C nanoparticle electrode at the large current density region, where a power density of 0.314 W cm −2 is achieved at 0.6 V.The poor power performance with rGO-based electrodes is in line with the dense electrode structure shown in the SEM analysis in Figure 1.To further understand the mechanisms behind the obtained performances, detailed analyses were conducted to obtain the ECSA, mass activity, and EIS of the involved electrodes (Figure 3); the results are summarized in Table 1.An acceptable ECSA value of 19.84 m 2 g −1 is obtained for the Pt/C electrode, which is ca.1/3 of the value obtained in the liquid half-cell rotating disk electrode (RDE) measurement (ca.50-70 m 2 g −1 ) and in line with values reported in the literature [15,19].However, the ECSA values observed for rGO-based electrodes are extremely low.By RDE measurement, the ECSA values obtained for Pt/rGO are usually similar to or even higher than Pt/C nanoparticle catalysts, but the value obtained here in the MEA is only 2.65 m 2 g −1 , which is much lower than that of Pt/C in the electrode.This lower ECSA for Pt/rGO further indicates a very low catalyst utilization ratio in the electrode (defined by the ratio of the ECSA observed in the electrode to the value by RDE measurement), ca.5.45%, taking into account the ECSA value of 48.62 m 2 g −1 reported by the RDE measurement [19], resulting from the stacking and overlapping of the rGO nanosheets in the catalyst layer.For the Pt(NW)Pd/rGO, the ECSA value drops from 19.07 m 2 g −1 by RDE measurement [15] to 2.97 m 2 g −1 here.Although the utilization ratio is still low, ca.15.59%, it has been much higher than Pt/rGO, resulting from the scaffolding effect of the nanowires.However, the utilization ratio is still much lower as compared with the Pt/C nanoparticles.In addition, an increase of the catalyst loading from 0.4 to 0.6 mgPt cm −2 leads to slightly reduced ECSA values, resulting from the mass transfer limitation mentioned above.The mass activity in the MEA was measured under pure O2 rather than air to reduce the influence of the mass transfer resistance in the catalyst layer [1,7].The standard To further understand the mechanisms behind the obtained performances, detailed analyses were conducted to obtain the ECSA, mass activity, and EIS of the involved electrodes (Figure 3); the results are summarized in Table 1.An acceptable ECSA value of 19.84 m 2 g −1 is obtained for the Pt/C electrode, which is ca.1/3 of the value obtained in the liquid half-cell rotating disk electrode (RDE) measurement (ca.50-70 m 2 g −1 ) and in line with values reported in the literature [15,19].However, the ECSA values observed for rGO-based electrodes are extremely low.By RDE measurement, the ECSA values obtained for Pt/rGO are usually similar to or even higher than Pt/C nanoparticle catalysts, but the value obtained here in the MEA is only 2.65 m 2 g −1 , which is much lower than that of Pt/C in the electrode.This lower ECSA for Pt/rGO further indicates a very low catalyst utilization ratio in the electrode (defined by the ratio of the ECSA observed in the electrode to the value by RDE measurement), ca.5.45%, taking into account the ECSA value of 48.62 m 2 g −1 reported by the RDE measurement [19], resulting from the stacking and overlapping of the rGO nanosheets in the catalyst layer.For the Pt(NW)Pd/rGO, the ECSA value drops from 19.07 m 2 g −1 by RDE measurement [15] to 2.97 m 2 g −1 here.Although the utilization ratio is still low, ca.15.59%, it has been much higher than Pt/rGO, resulting from the scaffolding effect of the nanowires.However, the utilization ratio is still much lower as compared with the Pt/C nanoparticles.In addition, an increase of the catalyst loading from 0.4 to 0.6 mg Pt cm −2 leads to slightly reduced ECSA values, resulting from the mass transfer limitation mentioned above.The mass activity in the MEA was measured under pure O 2 rather than air to reduce the influence of the mass transfer resistance in the catalyst layer [1,7].The standard measurement protocol defined by the U.S. Department of Energy (DOE) was followed [1].However, this test under oxygen still does not work very well for the Pt/rGO electrode, and a much lower mass activity of 0.016 A mg Pt −1 is observed as compared with 0.041 A mg Pt −1 for Pt/C.A similar value is also obtained for the catalyst loading at 0.6 mg cm −2 .For Pt(NW)Pd/rGO, this value reaches 0.044 A mg Pt −1 , even higher than Pt/C.The higher mass activity of this nanowire structure in the electrode can be ascribed to two factors: (i) the scaffolding effect, which partially mitigates the severe stacking of the 2D rGO nanosheets, thus improving the mass transfer performance; and (ii) the excellent specific catalytic activity from the special surface properties of the unique nanowires [6,8].
The improvement of the nanowire scaffolding effect and the mass transfer limitation of rGO-based electrodes are further confirmed in Figure 3b.The mass transfer impedance of Pt(NW)Pd/rGO is much lower than Pt/rGO, but still higher than Pt/C in the MEAs, as shown in Figure 3c.
Coatings 2018, 8, x FOR PEER REVIEW 6 of 9 activity of 0.016 A mgPt −1 is observed as compared with 0.041 A mgPt −1 for Pt/C.A similar value is also obtained for the catalyst loading at 0.6 mg cm −2 .For Pt(NW)Pd/rGO, this value reaches 0.044 A mgPt −1 , even higher than Pt/C.The higher mass activity of this nanowire structure in the electrode can be ascribed to two factors: (i) the scaffolding effect, which partially mitigates the severe stacking of the 2D rGO nanosheets, thus improving the mass transfer performance; and (ii) the excellent specific catalytic activity from the special surface properties of the unique nanowires [6,8].The improvement of the nanowire scaffolding effect and the mass transfer limitation of rGO-based electrodes are further confirmed in Figure 3b.The mass transfer impedance of Pt(NW)Pd/rGO is much lower than Pt/rGO, but still higher than Pt/C in the MEAs, as shown in Figure 3c.

Discussion
In the fabrication of PEMFC electrodes, the catalyst ink is coated onto the GDL or membrane surface.In the drying process, the organic solvent (e.g., IPA) in the catalyst ink is evaporated, leaving a porous catalyst layer [1,20].However, the 2D graphene nanosheets tend to stack on top of each other and overlap to form a dense structure within the catalyst layer, which blocks the diffusion of the reactant gas and the removal of the produced water in operating PEMFCs and causes poor power performance.Even by increasing the catalyst loading in the electrodes, an effective improvement of the power performance is not achieved because of the mass transfer limitation.Thus, the conclusion is usually drawn that 2D graphene-based materials are not suitable as catalyst supports for practical electrodes in PEMFC devices, despite the much better activities that were observed by the liquid half-  2a).Table 1.ECSA, specific (S.A.) and mass activities (M.A.) of the catalysts in membrane electrode assembly in single cells (derived from Figure 3a,b).

Discussion
In the fabrication of PEMFC electrodes, the catalyst ink is coated onto the GDL or membrane surface.In the drying process, the organic solvent (e.g., IPA) in the catalyst ink is evaporated, leaving a porous catalyst layer [1,20].However, the 2D graphene nanosheets tend to stack on top of each other and overlap to form a dense structure within the catalyst layer, which blocks the diffusion of the reactant gas and the removal of the produced water in operating PEMFCs and causes poor power performance.Even by increasing the catalyst loading in the electrodes, an effective improvement of the power performance is not achieved because of the mass transfer limitation.Thus, the conclusion is usually drawn that 2D graphene-based materials are not suitable as catalyst supports for practical electrodes in PEMFC devices, despite the much better activities that were observed by the liquid half-cell RDE measurement, where the influence of the mass transfer can nearly be ignored [16].
Nanowires have a large aspect ratio.When they are grown on a 2D nanosheet surface, the unique geometry can form scaffold-like structures and thus partially release the stacking influence of the nanosheets.In fact, in graphene-related research, this function has been used by Si et al. [18] to exfoliate graphene sheets by the use of Pt nanoparticles.In their work the presence of Pt nanoparticles impregnated on the surface of graphene showed a surface area (obtained by BET measurements) around 20 times larger than the graphene without Pt.This scaffolding effect in the nanowire/rGO electrode similarly improves the mass transfer performance within the catalyst layer and an even higher power density is achieved than with Pt/C at a low current density range (Figure 2a).However, the rGO nanosheets usually have a much larger size (on the micrometer scale, as shown in Figure 1 and [15]) than the length of Pt nanowires (usually 20-200 nm), so, along with the difficulty of nanowires covering the entire surface of every rGO nanosheet, the stacking of rGO still cannot be fully avoided.Therefore, the improvement of this scaffolding effect is still limited.The stacking and overlapping effects caused by the large rGO nanosheets dominates the structures of the electrodes; even with nanowires, large cracks can still not form as with Pt/C nanoparticle catalysts, and quite similar electrode structures are observed in SEM for electrodes made of both Pt/rGO and Pt(NW)Pd/rGO (Figure 1).When the fuel cell is operated at a large current density, as shown in Figure 2a, the amount of reactant gas required for the reaction and the water produced increased dramatically; thus, the scaffolding space provided by the aligned nanowires between the rGO nanosheets is insufficient and thus poor power performance is observed again.This finally causes a clear crossover of the polarization curves of the two MEAs from Pt(NW)Pd/rGO and Pt/C, as shown in Figure 2a.This also leads to another suggestion that if a large enough scaffolding effect can be introduced to the electrode structure to avoid the stacking and overlapping to form similar large cracks as that of Pt/C, e.g., by a further increase of the nanowire length and the improvement of their distribution on the rGO surface, or by reducing all rGO nanosheets to a relative smaller size, or through investigating new alternative electrode preparation methods [21,22], high power performance is still possible for rGO-based electrodes for PEMFCs in real-life operation.Such pursuits are of particular importance when considering the improved resistance of nanowires to coarsening in comparison to Pt/C nanoparticle catalysts [23,24] and the enhanced resistance of rGO supports to carbon corrosion [25], both major limitations in the commercial viability of PEMFCs.

Conclusions
In this work, we evaluated the catalyst electrodes made from Pt(NW)Pd/rGO and Pt/rGO in PEMFCs and the results were compared to Pt/C nanoparticle catalysts.The results demonstrated that the introduction of rGO-based catalysts tended to form a dense structure within the catalyst layer that limited the mass transfer in fuel cell operation and finally resulted in poor power performance.The aligned nanowires grown on rGO surface can work as a scaffold, thus improving the mass transfer limitation.At 0.6 V, power densities of 0.206 and 0.128 W cm −2 were obtained for Pt(NW)Pd/rGO and Pt/rGO electrodes, respectively, at the catalyst loading of 0.4 mg Pt cm −2 .The mass activity for Pt(NW)Pd/rGO was 0.044 A mg Pt −1 in MEA, which is much higher than 0.016 A mg Pt −1 of the Pt/rGO, and even better than 0.041 A mg Pt −1 for Pt/C.However, the power density obtained for the nanowire/rGO electrode is still lower than Pt/C at 0.6 V. Nevertheless, this work demonstrates the possibility of using graphene-based materials as a catalyst support for fuel cell devices.To really bring this technology into practical application, further study is required to understand the complicated influences of the nanowire length, distribution on rGO, size and structure of rGO, and electrode preparation method.

Figure 2 .
Figure 2. (a) Polarization and (b) power density curves obtained at a sweep rate of 1 mV s −1 at the cell temperature of 80 °C.The reactant gases are fully humidified H2 at the anode and air at the cathode with backpressure of 0.5/0.5 bars and stoichiometry of 1.3/2.4,respectively.

Figure 2 .
Figure 2. (a) Polarization and (b) power density curves obtained at a sweep rate of 1 mV s −1 at the cell temperature of 80 • C. The reactant gases are fully humidified H 2 at the anode and air at the cathode with backpressure of 0.5/0.5 bars and stoichiometry of 1.3/2.4,respectively.

Figure 3 .
Figure 3. (a) Cathode cyclic voltammetry (CV) scan between 0.05-1.2V at a sweep rate of 20 mV s −1 with a cell temperature of 80 °C.The reactant gases are fully humidified H2 at the anode and N2 at the cathode with backpressure of 0.5/0.5 bars and stoichiometry of 1.3/2.4,respectively.(b) Resistance and H2 crossover corrected polarization curves obtained at a sweep rate of 1 mV s −1 at the cell temperature of 80 °C.The reactant gases are fully humidified H2 at the anode and O2 at the cathode with backpressure of 0.5/0.5 bars and stoichiometry of 2/9.5, respectively.(c) EIS spectra at 0.65 V with amplitude 10 mV in the frequency range 10 kHz-0.1 Hz for cells with air as the reactant gas (the same settings as for Figure 2a).

Figure 3 .
Figure 3. (a) Cathode cyclic voltammetry (CV) scan between 0.05-1.2V at a sweep rate of 20 mV s −1 with a cell temperature of 80 • C. The reactant gases are fully humidified H 2 at the anode and N 2 at the cathode with backpressure of 0.5/0.5 bars and stoichiometry of 1.3/2.4,respectively.(b) Resistance and H 2 crossover corrected polarization curves obtained at a sweep rate of 1 mV s −1 at the cell temperature of 80 • C. The reactant gases are fully humidified H 2 at the anode and O 2 at the cathode with backpressure of 0.5/0.5 bars and stoichiometry of 2/9.5, respectively.(c) EIS spectra at 0.65 V with amplitude 10 mV in the frequency range 10 kHz-0.1 Hz for cells with air as the reactant gas (the same settings as for Figure 2a).

Table 1 .
ECSA, specific (S.A.) and mass activities (M.A.) of the catalysts in membrane electrode assembly in single cells (derived from Figure3a,b).