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Synergistic Mn-Co catalyst outperforms Pt on high-rate oxygen reduction for alkaline polymer electrolyte fuel cells


Alkaline polymer electrolyte fuel cells are a class of fuel cells that enable the use of non-precious metal catalysts, particularly for the oxygen reduction reaction at the cathode. While there have been alternative materials exhibiting Pt-comparable activity in alkaline solutions, to the best of our knowledge none have outperformed Pt in fuel-cell tests. Here we report a Mn-Co spinel cathode that can deliver greater power, at high current densities, than a Pt cathode. The power density of the cell employing the Mn-Co cathode reaches 1.1 W cm−2 at 2.5 A cm−2 at 60 oC. Moreover, this catalyst outperforms Pt at low humidity. In-depth characterization reveals that the remarkable performance originates from synergistic effects where the Mn sites bind O2 and the Co sites activate H2O, so as to facilitate the proton-coupled electron transfer processes. Such an electrocatalytic synergy is pivotal to the high-rate oxygen reduction, particularly under water depletion/low humidity conditions.


The recent decade has witnessed tremendous progress in both materials developments and catalysis studies of alkaline polymer electrolyte fuel cells (APEFCs)1,2,3,4,5,6,7,8,9. Research efforts have been driven by the fact that polymeric alkaline electrolytes can not only simplify the cell structure and operation, but also provide opportunities for employing non-precious metal catalysts10,11,12,13,14. However, despite great efforts, the last objective has remained elusive. While some materials, such as nitrogen-doped carbon-based materials15,16, have been suggested to exhibit Pt-comparable activity towards the oxygen reduction reaction (ORR) in alkaline media, their performance is still much lower than that of Pt in APEFCs17,18, especially when operated at high current densities necessary in automotive applications.

The screening of fuel-cell electrocatalysts is generally carried out using rotating disk electrode (RDE) voltammetry. However, the RDE experimental conditions are distinctly different from those in a polymer electrolyte fuel cell, where the electrode is fed with humidified gas, and the catalyst surface is under a humid atmosphere rather than in contact with an aqueous solution19, as is the case under RDE conditions. Thus, it is not surprising that good-performing electrocatalysts in RDE tests can often exhibit poor performance under fuel-cell operation.

Here, we report an unexpected finding that the Mn-Co spinel catalyst (denoted hereafter as MCS) exhibits activity that is inferior to that of Pt, for ORR in RDE tests, but superior performance in APEFC tests, in particular under low-humidity conditions. At 60 oC, the power density of APEFC employing such a MCS cathode reaches 1.1 W cm2 at 100 relative humidity (RH%) and 0.92 W cm−2 at 50 RH%, in comparison to 1 W cm2 at 100 RH% and 0.67 W cm−2 at 50 RH% for a Pt cathode. Through comprehensive characterizations, an unreported synergistic effect of the MCS surface is unraveled, where the Mn sites prefer O2 binding and the Co sites favor H2O activation. Such a mechanism is pivotal in APEFC cathode, where water is a reactant but usually depleted.


Electrochemical and fuel-cell tests

Figure 1a presents typical RDE profiles for the ORR catalyzed by Pt and MCS in 1.0 M KOH solution. A negative shift of 50 mV in the half-wave potential clearly indicates that the ORR occurs at a lower rate on MCS than on Pt, and this trend does not change with potential as evidenced in the Tafel plots (inset to Fig. 1a). Such an observation would usually lead to the conclusion that the MCS would not be a good choice as ORR electrocatalyst for APEFCs. However, the fuel cell tests tell a different, and most unexpected, story (Fig. 1b). An APEFC with a Pt-Ru anode and a Pt cathode, exhibiting a peak power density (PPD) of 1 W cm−2, is a benchmark of current APEFC research20,21. Upon replacing the Pt cathode with our MCS cathode, the cell performance underwent a slight loss at low current densities, but, as the current density increased, it kept increasing in a steady fashion, reaching a higher PPD of 1.1 W cm−2, a performance metric never previously achieved in APEFCs with a non-precious metal cathode catalyst to the best of our knowledge. The MCS cathode can even sustain a current density of 3.5 A cm−2, pointing to its inherently high activity.

Fig. 1

Comparison of Mn-Co spinel (MCS) catalyst and commercial Pt catalyst. a Rotating disk electrode (RDE) measurements in O2-saturated KOH solution (1 mol L−1) using 40 wt% Pt/C (Johnson Matthey, 50 μgPt cm−2) and 40 wt% MCS/C (72 μgmetal cm−2), respectively. Inset: Tafel plots. Scan rate = 5 mV s−1. Rotation rate = 1600 rpm. See Supplementary Figs 1 and 2 for relevant electrochemical data. bc Alkaline polymer electrolyte fuel cell (APEFC) tests with H2 and O2 at different relative humidities (RH). Anode catalyst: 60 wt% Pt-Ru/C (Johnson Matthey, 0.4 mgmetal cm−2). Cathode catalyst: 60 wt% Pt/C (Johnson Matthey, 0.4 mgPt cm−2) or 40 wt% MCS/C with an optimized loading of 0.58 mgmetal cm−2. (See Supplementary Fig. 3 for results with different catalyst loading.) Alkaline polymer electrolyte: aQAPS-S8 membrane (35 μm in thickness) and aQAPS-S14 ionomer (20 wt% in electrode)4. See Supplementary Figs 4 and 5 for impedance measurements and iR-corrected plots. Operation temperature = 60 °C. Backpressure = 0.1 MPa. d Performance comparison: Kinetic current densities (jk) at 0.85 V, calculated from the RDE data recorded in 1 mol L−1 NaOH/H2O and 1 mol L−1 NaOD/D2O (See Fig. S6 for relevant results of isotopic labeling experiments), and the peak power density (PPD) resulting from APEFC tests

Moreover, the MCS cathode dramatically outperforms the Pt cathode at low relative humidity over a wider range of current densities. As illustrated in Fig. 1c, when the humidity was lowered to 50 RH%, a significant drop in cell performance was observed for the Pt cathode, with the PPD decreasing by one third to 0.67 W cm−2. However, for the MCS cathode, the PPD remained virtually unchanged at 0.92 W cm−2. The ability to work at low relative humidity is a unique advantage for APEFC cathodes, where water (which is a reactant; vide-infra) is often depleted, particularly when the cell is operated at high current densities22. It should be noted that the Pt cathode has been well optimized to reach its maximum performance, the observed superiority of the MCS cathode, at high current densities and low humidity, is not due to a structural effect of the electrodes (including the thickness of the catalyst layer). In fact, the Pt cathode is thinner in the catalyst layer, which possesses lower electrical resistance than the MCS cathode (Supplementary Figs 4 and 5). Since the operation conditions (gas backpressure, flow rate, etc.) are the same for both electrodes, the mass transport should not be particular to the thinner Pt cathode. The obvious difference in the water/humidity dependence of the cathode performance has to be related to a certain catalyst-water interaction.

Figure 1d summarizes the activity comparison between Pt and MCS under different experimental conditions in RDE and fuel-cell tests. While Pt is superior, over the MCS, under water-rich conditions, it becomes inferior at low water content. This suggests the presence of an effect, on the ORR catalytic activity, that is sensitive to the water content and works oppositely on Pt and MCS. In APEFCs, H2O is not only necessary for ionic conduction, but is also a reactant in the ORR (Eq. 1).

$${\mathrm{O}}_2 + 2{\mathrm{H}}_2{\mathrm{O}} + 4e^ - \leftrightarrows 4{\mathrm{OH}}^ -$$

Proton transfer processes in this reaction are as crucial as the electron transfer events themselves23,24, as evidenced (via H/D isotope effects) by the significant diminution of the kinetics of the ORR in NaOD/D2O solution (Fig. 1d and Supplementary Fig. 6). Thus, the ORR will be highly sensitive to the amount, and state, of H2O just above the catalyst surface25,26, especially when H2O is a minority species in the gaseous phase. The high catalytic activity of MCS toward the ORR at low H2O content suggests the presence of a special affinity for H2O, in addition to the appropriate interactions with O2.

Material characterization

In an effort to unveil the origin of these effects, in-depth characterization of the structure and surface properties was carried out. Synchrotron X-ray diffraction (XRD, Fig. 2a) clearly indicates the presence of the cubic spinel structure (AB2O4)27 with a lattice constant a = 8.2938 Å. The formal valence of Mn and Co in the MCS sample exhibiting optimal ORR performance (nominally Mn1.5Co1.5O4) were analyzed using X-ray absorption near-edge structure (XANES, Fig. 2b), which yielded values of +2.76 and +2.56, respectively. The stoichiometry of the spinel (AB2O4) was thus determined to be [Mn0.3Co0.7][Mn0.6Co0.4]2O4, indicating that while Co is distributed almost uniformly at the tetrahedral (A) and octahedral (B) sites of the spinel lattice, Mn is enriched at the B site. The elemental ratio of Mn/Co is 3/2 at the catalytically active B site28. Scanning transmission electron microscopy (STEM) observations indicated that the MCS particles are irregularly-shaped nanocrystals (Supplementary Fig. 7). The high-angle annular dark-field STEM images (HAADF-STEM, Fig. 2c, d), taken on the [110] and [112] zone axes, provide atomic views of the arrangement of metal ions inside the MCS lattice. The high-contrast patterns match well the lattice model reconstructed based on the above-determined stoichiometry (see Supplementary Figs 8 and 9 for detailed interpretation). In addition, the atomic-scale elemental mapping, using energy-dispersive X-ray spectroscopy (Supplementary Fig. 10), also confirms the enrichment of Mn at the B sites.

Fig. 2

Structural characterizations of the Mn-Co catalyst. a Synchrotron X-ray diffraction (XRD) pattern, identifying the spinel cubic crystal structure with a lattice constant a = 8.2938 Å (inset). X-ray wavelength λ = 0.68876 Å. The raised baseline at around 10o is due to the carbon black support of the Mn-Co spinel (MCS). b X-ray absorption near-edge structure (XANES) spectra. The K-edge absorptions of Mn and Co were collected, each with three reference samples. The formal valences of Mn and Co were determined to be +2.76 and +2.56, respectively, corresponding to a stoichiometry of [Mn0.3Co0.7][Mn0.6Co0.4]2O4. c, d High-angle annular dark-field images from scanning transmission electron microscopy (HAADF-STEM) images of the MCS lattice, taken on zone axes of [110] and [112]. Models of lattice projection are provided, with a unit cell embedded in the picture, to interpret the atomic resolution images. See Supplementary Figs 8 and 9 for reasoning of the spot brightness. Elemental mapping results are provided in Supplementary Fig. 10

Surface analyses

In an attempt to distinguish the functionality of the Mn sites and Co sites on the spinel surface, we deliberately prepared MCS samples with Mn-segregated and Co-segregated surfaces, denoted as Mn-MCS and Co-MCS, respectively. The success in controlling surface segregation was ascertained by elemental mapping using electron energy loss spectroscopy (EELS, insets of Fig. 3a and Supplementary Figs 1113). Samples were then characterized with X-ray photoelectron spectroscopy (XPS) to identify the oxygen-containing surface species (Fig. 3a). In addition to O2− that constitutes the spinel, OHads and H2Oads were identified by their distinct chemical shifts29,30. While Mn segregation resulted in an enhancement in the O2– component and a diminution of H2Oads, Co segregation caused a reversal effect with a clear increase in the H2Oads component. These results suggest that the actual MCS surface consists mainly of Mn-OH/Mn-O and Co-OH/Co-OH2, in agreement with the zeta-potential analysis in solutions of varying pH. As shown in Fig. 3b, the potential of zero charge (PZC) of MCS appears at pH = 5.5, and shifts to pH = 8.5 upon Co segregation, and to pH = 3.3 upon Mn segregation. These observations suggest that the Co sites interact weakly with O, and tend to be positively charged, likely as Co-OH2δ+, while the Mn sites have a strong affinity for O, and tend to be negatively charged, likely as Mn-Oδ–.

Fig. 3

Surface analyses of the Mn-Co catalyst. a Oxygen 1 s spectra of X-ray photoelectron spectroscopy (XPS) for MCS and two reference samples with Mn or Co enriched on the surface (denoted as Mn-MCS and Co-MCS, respectively). Insets are electron energy loss spectroscopy (EELS) mapping for these samples (also see Supplementary Figs 1113). Spectral deconvolution identified three distinct chemical environments of O, corresponding to those of H2Oads, OHads, and O2–29,30. b Zeta-potential measurements for MCS, Mn-MCS, and Co-MCS particles dispersed in solutions of different pH. c Density functional theory (DFT) calculated adsorption energies for H2O, O2, and O on the Mn and Co sites of the MCS (100) surface, in comparison to those on Pt (111). No stable adsorption structure was found for O2 on the Co site of MCS (100). See Supplementary Tables 16 for Supplementary Data of DFT calculations. The adsorption energy of O was defined relative to half the energy of O2, such that negative values indicate a spontaneous dissociation of O2 on the surface

The above experimental observations of the surface character of the MCS are in qualitative agreement with density functional theory (DFT) calculations (Fig. 3c). The Mn sites on MCS are highly active for binding both O2 and H2O, but the Mn-O2 interaction is stronger than the Mn-OH2 interaction, suggesting that the Mn sites prefer to bind O2 over H2O when the MCS is exposed to humid air. In contrast, the Co sites have a notable affinity for H2O but appear not to bind O2 by itself (given that O2 can adsorb at the bridge sites between Mn and Co atoms, see Supplementary Table 1). Hence, when the MCS cathode is exposed to humid O2, the Mn sites and Co sites on the surface bind different adsorbates, preferentially yielding Mn-O2 and Co-OH2, respectively.

The DFT calculations can also provide an assessment of the capability of breaking the O-O bond at a catalytic site. Specifically, the adsorption energy of an O atom is calculated relative to half the energy of O2, such that negative values designate a thermodynamically spontaneous dissociation of O2. As presented in Fig. 3c, the dissociation of O2 is energetically highly favorable on the Mn site, but disfavored (albeit slightly) on the Co site. One can thus conclude that the MCS possesses a synergistic surface for ORR catalysis, with the Mn sites binding and cleaving O2, and the Co sites enriching and activating H2O, so as to facilitate the proton-coupled electron transfer processes of oxygen reduction.

Water activation in oxygen reduction

The proposed synergistic mechanism of the MCS-catalyzed ORR is illustrated, stepwise, in Fig. 4a. Assuming that Mn-OH and Co-OH represent the initial states, the O2 is preferentially bound to the Mn site to yield Mn-O2, along with a 1e reduction to produce OH. H2O is preferentially bound to the Co site, as Co-OH2, also with a 1e reduction to generate OH. A surface proton transfer (reaction I) can then occur from the Co-OH2 to the proximate Mn-O2, leading to a regenerated Co-OH and a Mn-OOH species that is followed by a 1e reduction to produce Mn=O and OH. The Mn=O can take the second proton, transferred from Co-OH2, to regenerate the Mn-OH (reaction II). The extraordinary feature of this mechanism includes the proton mediation by the turnover of Co-OH/Co-OH2 and the surface proton transfer between the proximate Co and Mn sites. On the one hand, based on DFT calculations, the O–H bond energy decreases from 5.14 eV to 3.42 eV when the H2O is bound to the Co site (upper-right inset of Fig. 4a). On the other hand, the energy barriers for reaction I and II are small (central inset of Fig. 4a, Supplementary Tables 7 and 8). We believe that these energetic features are fundamental to the H2O activation and proton-transferred reduction of O2 on the MCS surface.

Fig. 4

Reaction mechanism involving water activation. a Schematic illustration of the proposed synergistic mechanism of ORR on MCS, featuring the dissociative reduction of O2 at the Mn site, the proton mediation by the Co site, and the surface proton transfer in between (reactions I and II). Inset central: DFT-calculated energy barriers for reactions I & II on MCS (100) (See Supplementary Tables 7 and 8 for details). Inset upper-right: DFT-calculated bond energies of O–H in H2O and Co-OH2. b Results of in situ attenuated total reflection Fourier transform infrared (ATR-FTIR) studies for MCS and Pt electrodes in Ar or O2 saturated KOH solutions. See Supplementary Fig. 14 for relevant FTIR spectra. The IR signals of interest were from the bending vibration of H2O (inset). The Stark effect (wavenumber shift with potential) is a measure of the H2O adsorption on the surface. c Local density of water on MCS (100) and Pt (111) surfaces at 300 K, obtained from atomistic molecular dynamics (MD) simulations (also see Supplementary Fig. 15). Inset: Snapshots of water molecules in a surface layer up to 0.3 nm thick

To ascertain the involvement of surface H2O in the MCS-catalyzed ORR, in-situ attenuated total reflection Fourier transform infrared spectroscopy (ATR-FTIR) was employed to detect the subtle changes in the H2O vibrations on Pt and MCS surfaces under electrochemical conditions (Fig. 4b). The H2O bending vibration, δ(HOH), turns out to be at higher wavenumbers on Pt than on MCS, indicating that the Pt-H2O interaction is weaker than the MCS-H2O interaction31. Even more compelling evidence for the strong adsorption of H2O on the MCS surface is provided by the Stark effect, namely, a significant potential-dependent shift in the δ(HOH) wavenumber of 25 cm−1 V−1. In contrast, such a Stark effect is negligible on a Pt surface. These experimental observations are consistent with the DFT calculations (Fig. 3c) that show that the adsorption energy of H2O on Pt (111) is only one-third of that on MCS (100).

Additional valuable information was provided by in-situ ATR-FTIR experiments, showing that the δ(HOH) wavenumber decreased on both Pt and MCS when the atmosphere was switched from Ar to O2 (Fig. 4b). This can only be ascribed to the additional interaction between the surface H2O and the surface oxygen species, providing unambiguous evidence for the involvement of surface H2O in the ORR. Moreover, the δ(HOH) Stark effect remained unchanged on MCS during the ORR, indicating that the surface H2O has not been repelled by the co-adsorption of O2; whereas the originally weak Stark effect of δ(HOH) on Pt could barely be observed during the ORR, suggesting that the H2O is likely to be further away from the Pt surface when covered by oxygen species. The identification of the different functionalities of the Mn sites and Co sites, and the direct observation of the involvement of surface H2O in the MCS-catalyzed ORR, provide strong support for the synergistic mechanism (Fig. 4a).

The above computational and experimental observations clearly establish the superior activity of MCS over Pt for the ORR under conditions of high current density and low humidity. The lower ORR activity of MCS in RDE tests is also understandable. In O2-saturated KOH solutions, the molar ratio of H2O/O2 is over 104, so that the hydrophilic MCS surface is dominated by H2O32,33, despite the oxophilicity of the Mn sites. Molecular dynamics (MD) simulations (Fig. 4c) show that liquid water can wet the MCS surface with a proximity of 0.23 nm, in comparison to 0.3 nm on a Pt surface. Thus, there is more space for O2 adsorption on a Pt surface than on an MCS surface under water-flooding conditions.


Although MCS-like materials were used as ORR catalysts in the literature12,13,14, the mechanistic understanding has been vague and the cell performance observed here is unprecedented to the best of our knowledge. As for the stability, the MCS catalyst turns out to be more stable than Pt under the test protocol of potential cycling (Supplementary Fig. 16). Our findings represent not only the discovery of a practical, high-performance non-precious metal catalyst for APEFCs, but also reveal a strategy for the ORR catalyst design. In addition to the electronic effects that have often been used and/or invoked to tune the reactivity of solid surfaces toward O234,35, designing synergistic surfaces that can activate H2O and facilitate proton transfer processes is also pivotal for ORR catalysts, in particular for metal oxides working in alkaline media where both O2 and H2O are reactants.



Cobalt(II) acetate (Co(OAc)2·4H2O, 99.0%), manganese(II) acetate (Mn(OAc)2·4H2O, 99.0%), ammonium hydroxide (NH3·H2O, 25%-28%), potassium hydroxide (KOH, 99.99%), sodium hydroxide (NaOH, 99.99%) were purchased from China Medicine Shanghai Chemical Reagent Corporation. Sodium deuteroxide (40 wt% in D2O, 99 atom% D), deuterium oxide (D2O, 99.9 atom% D) were obtained from Sigma-Aldrich and used without further purification. Vulcan XC-72 (Cabot Co.), 60 wt% Pt/C (Johnson Matthey Co.), 60 wt% PtRu/C (Johnson Matthey Co.), Nafion (Dupont, 5%) were used as received. The alkaline polymer electrolytes (aQAPS-Sx) were prepared as reported in our previous work4.

Catalyst preparation

In a typical synthesis of Mn-Co spinel (MCS) catalyst supported on carbon black, Co(OAc)2·4H2O (63.5 mg) and Vulcan XC-72 (preheated at 110 oC in air, 60.0 mg) were added to ultrapure water (30 mL). After ultrasonic blending for 15 min, 0.5 mL of NH3·H2O was added under magnetic stirring, followed by the addition of Mn(OAc)2·4H2O aqueous solution (62.5 mg dissolved in 5 mL water). The mixture was aged at a controlled temperature under magnetic stirring for 2 h. After that, the suspension was ultrasonically blended for 10 min, and then transferred to a 40 mL Teflon autoclave for hydrothermal reaction at 150 oC for 3 h. The resulting product was collected by centrifugation and washed with water, then freeze dried under vacuum. To ensure a homogeneous distribution of Co and Mn in MCS, the ageing temperature must be set to 60 oC. To prepare MCS with Mn segregation on the surface (denoted as Mn-MCS), the ageing temperature was set to 40 oC; while to prepare Co-segregated samples (Co-MCS), the heating was set to 80 oC before the addition of Mn(OAc)2 aqueous solution. MCS samples without carbon black support were synthesized employing the same procedure without the addition of Vulcan XC-72.

Electrochemical measurements

To prepare the working electrode, a 5 mg sample was dispersed ultrasonically in 1 mL of diluted Nafion alcohol solution (0.05 wt%) to form an ink, and the suspension was pipetted onto a rotating ring-disk electrode (RRDE, ϕ = 4.57 mm), which was buff-polished with an alumina suspension (ϕ = 0.05 μm) prior to use. The catalyst coated electrode was dried under an infrared lamp. aQAPS ionomer was also tested as the binder, no difference was found from using Nafion ionomer.

Electrochemical experiments were conducted on a CHI-700A potentiostat with an RRDE system (Pine Research Instruments). A sheet of carbon paper (Toray) was used as the counter electrode. Hg/HgO in the same solution was used as the reference electrode, and all potentials were converted to the reversible hydrogen electrode (RHE) in the same solution. The oxygen reduction reaction (ORR) evaluation was carried out in O2-saturated 1.0 M KOH solution. The rotation rate was 1600 rpm, and the ORR curves were recorded by cycling the potential between 0.40 V and 1.05 V (vs. RHE) at 5 mV s−1. The kinetic current densities and Tafel plots were calculated by the average current densities of positive and negative scans. Cyclic voltammetry (CV) was carried out in Ar-saturated 1.0 M KOH solution by cycling the potential between 0.10 V and 1.40 V (vs. RHE) at different scan rates. All measurements were carried out at 25 oC.

The kinetic current densities (jk) were calculated via Koutecky-Levich analysis:

$$\frac{1}{j} = \frac{1}{{j_{\mathrm{k}}}} + \frac{1}{{j_{\mathrm{d}}}}$$

where j is the total current density, and \(j_{\mathrm{d}} = 0.62nFD_{{\mathrm{O}}_2}^{2/3}\omega ^{1/2}\nu ^{ - 1/6}C_{{\mathrm{O}}_2}^ \ast\) is the diffusion limiting current density (n = electrons transferred number, F = Faraday’s constant, \(D_{{\mathrm{O}}_2}\) = diffusion coefficient of O2, ω = electrode rotation rate, ν = kinematic viscosity, \(C_{{\mathrm{O}}_2}^ \ast\) = the bulk concentration of O2).

To evaluate the H2O2 yield and the electron transfer number of the catalysts, the Pt ring potential was set to 1.3 V (vs. RHE) in the RRDE measurements. The H2O2 yield was calculated using the following equation36:

$${\mathrm{H}}_2{\mathrm{O}}_2(\% ) = 200 \times \frac{{I_{\mathrm{R}}/N_0}}{{(I_{\mathrm{R}}/N_0) + I_{\mathrm{D}}}}$$

Where IR and ID are the ring and disk currents, respectively, and N0 = 0.22 is the collection efficiency of the RRDE.

Isotopic labeling experiments

To study the kinetic isotope effect (KIE), 1.0 M NaOH and 1.0 M NaOD solutions were prepared with Milli-Q water (>18 MΩ cm) and D2O, respectively. All vessels were dried under an infrared lamp before used, and the catalyst coated electrodes were soaked in the electrolyte solution for 30 min. before electrochemical experiments. The electrochemical experiments were conducted using the same procedure described above.

The KIE is the ratio of the rate constants (\(k_f^H/k_f^D\)), which can be calculated at a selected potential37

$${\mathrm{KIE}} = \frac{{k_f^H}}{{k_f^D}} = \frac{{j_{\mathrm{k}}^Hn^DFC_{{\mathrm{O}}_2}^{ \ast ,D}}}{{j_{\mathrm{k}}^Dn^HFC_{{\mathrm{O}}_2}^{ \ast ,H}}}$$


$$\frac{{C_{{\mathrm{O}}_2}^{ \ast ,D}}}{{C_{{\mathrm{O}}_2}^{ \ast ,H}}} = 1.101\quad \quad (298\,{\mathrm{K}})$$

due to the difference in the solubility of O2 in D2O and H2O. By assuming that the electron count (number of electrons transferred) (\(n^D = n^H\)), the KIE can then be calculated as

$${\mathrm{KIE}} = \frac{{k_f^H}}{{k_f^D}} = \frac{{j_{\mathrm{k}}^HC_{{\mathrm{O}}_2}^{ \ast ,D}}}{{j_{\mathrm{k}}^DC_{{\mathrm{O}}_2}^{ \ast ,H}}} = 1.101\frac{{j_{\mathrm{k}}^H}}{{j_{\mathrm{k}}^D}}$$

The ORR KIEs on Pt and MCS at +0.85 V (vs. RHE) were calculated to be 2.08 ± 0.2 and 2.14 ± 0.2, respectively, both belonging to a primary isotope effect38.

Fuel cell tests

The procedures for fabricating membrane-electrode assemblies and fuel cell tests were the same as reported previously20. Specifically, the catalyst powder was dispersed in a aQAPS-S14 (Cl as anion) ionomer solution and sprayed onto each side of an aQAPS-S8 (Cl as anion) membrane (35±5 µm in thickness) to fabricate the catalyst coated membrane (CCM). The area of electrodes was 4 cm2. The catalyst loadings for PtRu/C in the anode and Pt/C in the cathode were 0.4 mgmetal cm−2. Different MCS loadings in the cathode were tested to find the optimal value. The weight percentage of aQAPS-S14 in the electrodes was controlled to be 20 wt%. To replace the Cl anion in the CCM to OH, the CCM was immersed in 1.0 M KOH solution for 10 h. Finally, the CCM in the OH form, was repeatedly rinsed with deionized water until the pH of the residual water was neutral. It was then pressed between two pieces of carbon paper (AvCard GDS3250) to make the membrane-electrode assembly (MEA).

The H2-O2 fuel cells were tested (850e Multi Range, Scribner Associates Co.) under galvanic mode using humidified H2 and O2 gases. The cell temperature was set to 60 oC, and the flow rate of both H2 and O2 gases was 200 mL/min with 0.1 MPa of backpressure. To obtain 50 RH% of H2 and O2, the temperature of the humidifying water tanks was set as 45.7 oC.

Synchrotron X-ray measurements

Synchrotron X-ray diffraction (XRD) and X-ray absorption spectroscopy (XAS) measurements were conducted at the Taiwan Beam Line of BL12B1 in the Spring-8. The electron-storage ring was operated at 8 GeV with a current of 100 mA. For the XRD measurements, the MCS/C samples were placed in a glass capillary and sealed with a resin. The wavelength of the incident X-ray beam was set to 0.68876 Å, which was calibrated with a CeO2 standard. XRD data were recorded on an imaging plate for 30 min over the range 2θ = 0–40o with a 2θ step of 0.01o.

For the XAS measurements, a Si (111) double-crystal monochromator was employed for the energy selection with a resolution dE/E better than 2 × 10−4 at elemental edges. All XAS spectra were recorded at room temperature in transmission mode. Higher harmonics were eliminated by detuning the double-crystal Si (111) monochromator. Three gas-filled ionization chambers were used in series to measure the intensities of the incident beam (Io), the beam transmitted by the sample (It), and the beam subsequently transmitted by the reference foil (Ir). The third ion chamber was used in conjunction with the reference metal foil for the elemental edge measurements. All measurements were compared against the reference samples. The X-ray absorption near-edge structure (XANES) was fitted by a linear combination with the spectra of standards, within a range of −20 to 30 eV of the E0-normalized spectra, using the Athena software39. The oxidation state of Mn was fitted by a linear combination of MnO, Mn3O4, and LiMnO2, while the oxidation state of Co was fitted by a linear combination of CoO, Co3O4, and LiCoO2.

Electron microscopy analysis

Scanning transmission electron microscopy (STEM) imaging and energy-dispersive X-ray spectroscopy (EDX) mapping were acquired on a JEOL JEM-ARM200CF microscope operated at 80 kV with a Schottky cold-field emission gun in Wuhan University. The high angle annular dark field (HAADF) images were acquired with a beam convergence angle of 31 mrad. The EDX elemental mapping was carried using the JEOL SDD-detector with two 100 mm2 X-ray sensor. The STEM imaging with electron energy loss spectroscopy (EELS) elemental mapping was acquired on a fifth-order aberration-corrected FEI Titan Themis operated at 60 keV at Cornell University. Atomic-scale EELS elemental mapping was acquired on a fifth-order aberration-corrected Nion UltraSTEM operated at 60 keV. Beam damage of sample was routinely examined before and after EELS mapping.

Element and surface analyses

Inductively coupled plasma optical emission spectrometry ICP-OES (IRIS Intrepid II XSP, Thermo) was used to determine the Mn and Co contents in the MCS samples. The X-ray photoelectron spectroscopy (XPS) data were collected on a Thermo Fisher EscaLab 250Xi spectrometer using Al Kα radiation (h = 1486.6 eV). The O 1 s spectra were fitted using the XPSPEAK41 software. Zeta-potential measurements were carried out on Malvern Zetasizer Nano ZSP equipped with a pH autotitrator. 10 mg MCS samples without carbon supporters were dispersed in 100 mL KCl solution (1 mmol L−1) to obtain stable stock solutions for the subsequent measurements.

In-situ infrared spectroscopy

A Au film was prepared on the reflecting plane of an attenuated total reflection (ATR) Si prism by a secondary chemical deposition technique40. The thin Au film exhibited a surface-enhanced infrared absorption (SEIRA), which is very sensitive to the detection of surface absorbed species41. The catalyst ink was pipetted onto the Au film, dried under an infrared lamp. The MCS and Pt loadings were 50 µg/cm2. The IR beam traveled through the Si prism with an incident angle of 70° to detect the surface absorption species on the working electrode by an evanescent infrared wave and finally arrived at the detector through the total reflection. An FTIR spectrometer (Thermo Fisher Nicolet 6700) equipped with an MCT detector was used for ATR-SEIRAS measurements. The spectral resolution was set to 8 cm−1 and 64 interferograms were co-added for each spectrum. All IR spectra are presented in absorbance units, defined as −log (I/I0), where I and I0 represent the spectral intensities of the sample and reference states, respectively. The reference spectra were collected at 1.2 V (vs. RHE) under Ar or O2 atmosphere.

Density functional calculations

Density functional theory (DFT) calculations were performed using the Vienna Atomic Simulation Package (VASP, version 5.3)42. Generalized gradient approximation (GGA) of Perdew-Burke-Ernzerhof (PBE) was supplemented by the rotationally invariant “+U” description43. A projected augmented wave (PAW) basis, along with a plane-wave kinetic energy cutoff of 400 eV, was used throughout. The Hubbard U values of Mn and Co atoms were chosen as 4.4  eV and 5.4 eV, respectively44. Spin polarization calculations were carried out for all possible structures. For the calculation of surface and chemisorption systems, the spinel (100) surface was constructed as an eight-layer atom slab and repeated in super cell geometry with successive slabs separated by a vacuum region (10 Å). During the geometry optimization, the adsorbate layer and the top four layers of the slab were allowed to relax. For the calculations of surface and chemisorption systems of Pt, a Pt (111) surface was constructed as a four-layer metal slab. During geometry optimization, the adsorbate layer and the top two layers of the slab were allowed to relax. The energies were converged to 1 meV per atom and ionic relaxations were allowed until the absolute value of the force on each atom was below 0.02 eV Å−1. Minimum energy pathways (MEPs) were obtained by the climbing image nudged elastic band (CI-NEB) method with a force convergence to 0.03 eV Å−1.

Molecular dynamics simulations

Classical atomistic molecular dynamics (MD) simulations were carried out using Gromacs45. The simulation was carried out in the NVT ensemble. The temperature was kept at 300 K using the Nosé-Hoover thermostat46. The cut-off for short-range interactions was 1.2 nm and the particle-mesh Ewald method was used to account for long-range electrostatics. A time step of 2 fs was used for the simulation. We carried out a 5 ns simulation with the coordinates saved every 1 ps.

The surfaces of Pt(111) and MCS(100) were directly taken from the equilibrium structures in DFT calculations. For the Pt surface, a simple Lennard-Jones potential was used. This potential has been widely used in various systems with water47. For the MCS surface, the universal force field was used48. The Chargemol program49 was used to describe the DDEC6 atom charges, which can reproduce the electrostatic potential from DFT simulations. For water, we used the SPC/E model50. The Lorentz-Berthelot mixing rules were invoked for all interspecies interactions.

The box had a width and length of 4.7 and 6.2 nm, respectively, to match the lattice constants of Pt and MCS surfaces. The two surfaces were separated by a 10-nm water layer and fixed in their initial positions. The height of the box was chosen to be 15 nm so that a wide vacuum layer was generated on the other side to avoid influences between the two surfaces.

The radial distribution function was calculated for the oxygen atom in water around the metal atoms in the surface of Pt or MCS.

Data availability

The source data underlying Figs 1, 2a, b, 3a, b and 4b, c are provided as a Source Data File. All relevant data are also available from the authors.


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This work was financially supported by the National Key Research and Development Program of China (2016YFB0101203) and the National Natural Science Foundation of China (91545205, 21872108). This work made use of TEM facilities of the Cornell Center for Materials Research (CCMR), which are supported through the National Science Foundation Materials Research Science and Engineering Center (NSF MRSEC) program (DMR-1719875), and the Center for Alkaline Based Energy Solutions (CABES) funded by the U.S. Department of Energy under Award DE-SC0019445.

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Y.W. performed electrochemical experiments and DFT calculations; Y.Y., S.J. and H.Z. performed TEM experiments; Y.Y. and X.-m.W. performed synchrotron X-ray experiments; K.L. performed MD simulations; Y.P. performed polyelectrolyte synthesis; X.W. performed FTIR measurements; H.R. performed complementary experiments; J.W., D.A.M., B.J.H., and J.L. performed the analysis of experimental data; L.X., H.D.A., and L.Z. supervised the whole work and wrote the paper.

Corresponding authors

Correspondence to Li Xiao, Héctor D. Abruña or Lin Zhuang.

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Wang, Y., Yang, Y., Jia, S. et al. Synergistic Mn-Co catalyst outperforms Pt on high-rate oxygen reduction for alkaline polymer electrolyte fuel cells. Nat Commun 10, 1506 (2019).

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