Shangkun
Jiang‡
abc,
Qiong
Xiang‡
ab,
Zhuoyang
Xie
ab,
Na
Yang
d,
Jiawei
Liu
e,
Li
Li
*ab and
Zidong
Wei
*ab
aState Key Laboratory of Advanced Chemical Power Sources (Chongqing University), China. E-mail: liliracial@cqu.edu.cn; zdwei@cqu.edu.cn
bSchool of Chemistry and Chemical Engineering, Chongqing University, Chongqing, 400044, China
cCollege of Chemistry and Chemical Engineering, Chongqing University of Science &Technology, Chongqing, 401331, China
dSchool of Materials and Energy, University of Electronic Science and Technology of China, Chengdu, 611731, China
eInstitute of Sustainability for Chemicals, Energy and Environment (ISCE2), Agency for Science, Technology and Research (A*STAR), 627833, Singapore
First published on 5th November 2024
Understanding the Pt/ionomer/water interface structure and its impact on the oxygen reduction reaction (ORR) activity is essential for enhancing catalyst utilization and performance of fuel cells. This study aimed to investigate the influence of sulfonic acid groups on the Pt/ionomer/water interface and the ORR mechanism. By using a combination of DFT, AIMD, and microkinetic simulations, the results showed that when the sulfonic acid group is located at the edge of the Helmholtz plane, it creates an optimal three-phase interface, providing more available active sites, a stronger interfacial electric field, and a more continuous H-bond network. This configuration results in the *OOH dissociation becoming the rate-determining step, demonstrating significantly higher intrinsic ORR activity with a much lower theoretical overpotential of 0.11 V. Conversely, when the sulfonic acid group is in contact with the Pt surface, it causes the Pt surface's d-band center to shift down, weakens the interfacial electric field, and disrupts the H-bond network, resulting in a blocking effect on the ORR with an overpotential of 0.23 V. These insights shed light on the role of solid–solid–liquid interfaces in the ORR performance and provide valuable information for the rational design of catalyst interfaces.
The sulfonic acid groups inherent in Nafion ionomers are vital in enhancing proton transfer at the three-phase interfaces within the MEA. However, during the ORR, Nafion's adsorption and subsequent coverage can impede the crucial transport and diffusion of oxygen across the catalyst surface. This obstruction ultimately diminishes the catalytic efficiency, leading to a decrease in both the mass activity and peak power density of the MEA.14–16 Wang et al.17 quantified both local and bulk resistances of O2 by employing limiting current measurements and linear extrapolation, respectively. Their findings indicate that local resistance of O2 dominates the overall resistance of O2 within the MEA. Furthermore, the sulfonic acid groups in Nafion may occupy the active sites present on the Pt catalyst surface, leading to catalyst poisoning and a decrease in catalytic activity.18 Kodama et al.19 demonstrated that the dehydration of the ionomers enhances the adsorption of sulfonic acid groups on the Pt(111) surface, severely impairing the ORR performance under operating conditions, especially in comparison to well-hydrated conditions. Additionally, strong adsorption of these groups impedes the mobility of Nafion's side chains, further increasing the mass transfer resistance for water.20,21
To mitigate the catalyst poisoning caused by sulfonic acid groups and enhance the oxygen transport rate, strategies have been devised, including solvent regulation,22 ionomer modification,15,23 and innovative support materials.24,25 Chen et al.22 effectively reduced the adsorption of sulfonic acid groups on Pt surfaces using cyclohexanol, creating a non-contact interface between Pt and Nafion. This method significantly decreased sulfonic acid group coverage on Pt, improving reaction kinetics and reducing mass transfer resistance. Zhang et al.26 employed steric hindrance through a porous covalent organic framework to lessen the ionomers' encapsulation of the Pt/C catalyst and minimize direct interactions between sulfonic acid groups and Pt, thus enhancing mass activity and peak power density by a factor of 1.6. Cheng et al.27 demonstrated that the introduction of nanopores onto/within the Nafion film significantly reduced the local oxygen transport resistance by 78%, from 0.37 s cm−1 to 0.08 s cm−1, ultimately enhancing the performance of fuel cells. Additionally, Yarlagadda et al.24 used ordered mesoporous carbon as a carrier to prevent Nafion coverage on Pt surfaces, effectively reducing mass transfer resistance for protons and oxygen. However, the specific mechanisms of how sulfonic acid groups interact with catalysts and their role in inducing catalyst poisoning, as well as their impact on the structure and performance of the three-phase interface, remain largely unexplored at present. Additionally, the presence of ionomers at the three-phase interfaces significantly impacts the electrical double layer28–33 and alters the electronic structure of the catalyst surface.34,35 This complicates the ionomer–catalyst interfaces, making it difficult to comprehend their interactions and catalytic processes. Therefore, more research is needed to better understand the ionomer–catalyst interactions, reveal its underlying block mechanism for the ORR, and then develop effective strategies for regulating ionomer distribution in the MEA.
This work combines density functional theory (DFT) and ab initio molecular dynamics (AIMD) simulations to investigate how the sulfonic acid groups of ionomer side chains influence the three-phase interfaces of Pt/ionomers/water. The focus is on their impact on the electric double-layer structure and ORR activities. The configurations of ionomer side chains at different distances from the Pt(111) surface are screened to determine their interaction. Then, the electronic structure of the Pt(111) surface, along with the distribution of water molecules and hydrogen bonds (H-bonds) within the Helmholtz plane(HP), is analyzed. In the end, the free energy of the elementary steps and the linear scanning curve (LSV) of the ORR are simulated to evaluate the activity of the Pt/ionomer/water interface. The study identifies an ideal Pt/ionomer/water interface structure with high intrinsic ORR activity, provides valuable insights into the underlying blocking effect of Pt–ionomer interaction on the ORR, and underscores the crucial role of the solid–solid–liquid interfaces in ORR performance.
DFT was implemented in the Vienna Ab Initio Simulation Package (VASP) code.39 The projector-augmented wave (PAW) pseudopotential method was used to describe the electron–ion interactions,40 and the generalized gradient approximation (GGA) of the revised Perdew–Burke–Ernzerhof (RPBE) functional determined the electron exchange–correlation energy.41 The cutoff energy of the basis set of plane waves was 450 eV, and Monkhorst–Pack k-point meshes of (3 × 3 × 1) were selected for k-space integration. The calculation cannot be stopped until the system energy and force converge within 10−5 eV and 0.01 eV Å−1, respectively. AIMD is based on a canonical (NVT) ensemble, maintaining a constant temperature of 400 K by the Nosé–Hoover thermostat method, where the timestep was set to 1 fs. Initial dynamic pre-optimization over 2 ps ensures kinetic equilibrium, followed by a 10 ps steady-state simulation, from which 10000 frames are statistically analyzed.
Subsequently, solvent water molecules are involved in the system to simulate the Pt/ionomer/water interfaces. After conducting AIMD steady-state simulation (Fig. S2†), shown in Fig. 1b, the water molecules tend to interact with Pt atoms and the sulfonic acid group, leading to a slight increase in the distance between Pt and the sulfonic acid group. In Fig. 1c, the statistical distance between Pt and the sulfonic acid group shows that in the contact structure, the DPt–S fluctuates between 3.0 Å and 4.2 Å and is mainly located at 3.6 Å, and the DPt–O varies between 1.8 Å and 3.8 Å, with peak location of 2.8 Å. They are much shorter than those in the non-contact structure; that is, the DPt–S and DPt–O are mainly located at 5.0 Å and 4.2 Å, respectively. This indicates that the sulfonic acid group in the contact structure still interacts more strongly with Pt than it does in the non-contact structure.
The charge transfer, E-Fermi, and WF further confirm the interaction mentioned above. In Fig. 1d, the interaction between Pt(111) and the sulfonic acid group in the contact structure leads to a transfer of charge from Pt(111) to the sulfonic acid group, resulting in more electron deficiency of surface Pt atoms, exhibiting less negative Bader charge (−0.02 e per atom) and a downshifted d-band center (Fig. S3(b)†). In the non-contact structure, only the charge transfer between Pt and water causes the surface Pt atoms to show a more negative Bader charge (−0.04 e per atom) with less electron deficiency and a higher d-band center. Correspondingly, the contact structure displays a lower E-Fermi and a larger WF due to the fewer redundant electrons on the surface Pt atoms compared to the non-contact structure. At the same time, as shown in Fig. 1e, the interaction of the Pt–sulfonic acid group reduces the difference in electrostatic potential between Pt and electrolyte, while the non-contact structure shows an increased electric field strength. In short, the electronic structures observed under vacuum and solvent conditions show a similar trend. Solvent models differ slightly due to explicit water, weakening Pt–sulfonic acid group interactions, and reducing charge transfer.
These variations in the Pt/ionomer/water interface are primarily influenced by the positioning of the sulfonic acid groups. In Fig. S4,† the RDF peaks of the sulfonic acid group in the contact structure suggest that the group is positioned within the IHP, leading to a reduction in water density and weakened water adsorption. This can be attributed to the large charge transfer from the Pt to the sulfonic acid group in the contact structure, which downshifts the d-band center of Pt(111), weakens species adsorption, and reduces the density of the active sites (Fig. S5†). Conversely, in the non-contact structure, the sulfonic acid groups are predominantly situated on the edge of the OHP, exerting less influence on the water structure in the HP.
Furthermore, the orientation distributions of water in the HP are depicted in Fig. 2c and d. In the IHP, the adsorbed water molecules predominantly align with H-up (θ = 0° to 60°) and H-parallel (θ = 60° to 120°) orientations due to the interaction between Pt and water. On the other hand, the interfacial water molecules are predominantly characterized by H-parallel and H-down (θ = 120° to 180°) orientations. The concentration and orientation of water molecules differ between the contact and non-contact structures. In Fig. S6,† the contact structure contains fewer water molecules and a relatively concentrated H-parallel orientation. The non-contact structure has a larger number of water molecules with a more dispersed orientation, mainly concentrated in the H-up to the H-parallel orientations.
Additionally, 2D density distribution maps of the H-bond in Fig. 2e and f show that the H-bond of the contact structure is mainly concentrated in the IHP, while the non-contact structure has a higher number of H-bonds in both the IHP and the OHP, resulting in a wider distribution and continuous H-bond network. Specifically, the number of H-bonds in the HP of non-contact structures is approximately double that of contact structures, as shown in Fig. S7.† The length of the H-bond in the IHP of the non-contact structure is slightly more concentrated and shorter than that of the contact structure. This discrepancy is also attributed to the interaction of the sulfonic acid group in the contact structure with Pt and adsorbed water, which weakens the H-bond between them and disrupts the H-bond network.
Fig. 3b illustrates the change in free energy for the diffusion of O2 from the outside of the HP, at a distance of 5.0 Å, to the inside of the HP, at a distance of 2.5 Å. The corresponding snapshots of solvated structures are shown in Fig. S8 and S9.† The free energy first increases and then decreases as O2 moves closer to the Pt surface, indicating that overcoming a barrier is necessary for oxygen diffusion into the HP. The O–O bond length oscillates around the equilibrium bond length of 1.23 Å without activation. The energy barriers for O2 diffusion in the contact and non-contact structures are 0.18 eV and 0.15 eV, respectively. This suggests that there is a relatively small difference between these two structures in the diffusion resistance by the HP. However, the lower final state energy in the non-contact structure indicates a stronger interaction of its Pt surface with O2. In other words, the sulfonic acid group in the contact structure blocks the Pt surface from attracting and stabilizing reactants.
Due to the interaction between the Pt surface and O2, as shown in Fig. 3c, the adsorption of O2 is a spontaneous process with a slight decrease in the free energy. Subsequently, the protonation of *O2 to form *OOH requires overcoming the energy barrier accompanied by the elongation of the O–O bond from 1.23 to 1.40 Å. The formation of *OOH in the non-contact structure exhibits much lower energy barriers and a more stable final state compared to that in the contact structure. The snapshots of O2 protonation structures are shown in Fig. S10 and S11.† It can be attributed to the strong interaction between Pt and species and the well-connected H-bond network in the non-contact structure, which benefits proton transfer and stabilization of intermediates.
For the same reason, in the non-contact structure, the following ORR steps, including the dissociation of *OOH, the protonation of *O, and the desorption of *OH, have significantly lower energy barriers compared to the contact structure. For example, in Fig. 3d, the dissociation energy barrier of *OOH in the non-contact structure is 0.29 eV because the well-connected H-bond network benefits the proton transfer and the strengthened interfacial electric field improves the activation of the *O–OH bond, whereas, in the contact structure, it is as high as 0.60 eV. The snapshots of the dissociation of *OOH structures are shown in Fig. S12 and S13.† Additionally, in Fig. 3e and f, the protonation of *O and *OH and the following desorption in the non-contact structure (Fig. S15 and S17†) occur almost spontaneously with energy barriers of less than 0.05 eV, while in the contact structure (Fig. S14 and S16†), these steps require 0.31 and 0.15 eV, respectively.
Fig. 4a summarizes all energy barriers of the ORR elementary step in both contact and non-contact structures. Contrary to what thermodynamic calculations in vacuum suggest about the ORR's potential-determining step (PDS) being the desorption of OH,42 the rate-determining step (RDS) at the Pt/ionomer/water interface is the protonation and dissociation step of *OOH. This means that the presence of a solution can decrease the adsorption strength of species on the Pt surface and promote the protonation and desorption of OH during the ORR. In the non-contact structure, the energy barriers for each step are consistently lower than those in the contact structure. However, the steps involving adsorption and proton transfer in the contact structure have much higher reaction energy barriers. Utilizing the RDS energy barriers, exchange current densities are calculated and presented in Fig. 4b. The exchange current density for the non-contact structure is 2.87 × 10−5 A cm−2, approximately 100 times higher than that in the contact structure (3.21 × 10−7 A cm−2), underscoring the superior ORR activity of the non-contact structure. Considering the cathodic potential, species coverage, and active site density, the LSV curves were fitted by microkinetic simulations shown in Fig. 4c. The half-wave potential and onset potential for the contact structure are 0.93 V and 1.00 V (vs. RHE), respectively. The half-wave potential and onset potential for the non-contact structure are increased to 1.05 V and 1.12 V (vs. RHE), respectively. The much lower theoretical overpotential demonstrates that the non-contact structure is the ideal three-phase interface exhibiting much higher intrinsic ORR activity.
Fig. 4 (a) Energy barriers for each step of the ORR; (b) exchange current density; (c) the simulated LSV curve for both contact and non-contact structures. |
Therefore, the ideal Pt/ionomer/water interface involves having the ionomer located at the edge of the OHP. This arrangement helps to reduce the poisoning of sulfonic acid groups on active sites while also strengthening the interfacial electric field and forming a more continuous H-bond network. These factors are conducive to oxygen adsorption, activation, and protonation. Specific strategies, including selecting suitable dispersants, adjusting the pore structure of carbon supports, and modifying the structure of sulfonic acid groups, among others, can regulate the distance between the sulfonic acid groups and the catalyst surface. If the ionomer is located within the IHP, it has a blocking effect on the ORR by decreasing the surface redundant electrons, lowering the d-band center, weakening the interfacial electric field, and disrupting the H-bond network of the HP. These changes hinder species adsorption and O–O bond activation, impede proton transfer, and ultimately reduce the intrinsic activity of the ORR.
Footnotes |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4sc06600f |
‡ These authors contributed equally to this work. |
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