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Proceedings of the National Academy of Sciences of the United States of America logoLink to Proceedings of the National Academy of Sciences of the United States of America
. 2019 Mar 28;116(16):7611–7613. doi: 10.1073/pnas.1903412116

Theory and experiments join forces to characterize the electrocatalytic interface

Stephan N Steinmann a, Zi-Yang Wei b, Philippe Sautet b,c,d,1
PMCID: PMC6475385  PMID: 30923115

Electrocatalysis is gaining impetus as a key technology in fuel cells and for the medium-term energy storage in the context of intermittent, renewable energy sources such as wind and solar power. Furthermore, electrocatalysis promises to convert rather inert molecules such as CO2 and N2 into reduced products such as CO and ammonia under relatively mild conditions (1, 2). Harnessing the full power of electrocatalysis is, however, hampered by a lack of understanding of the governing physical and chemical processes at the metal–electrolyte interface. In PNAS, Cheng et al. (3) bring key insight to the characterization of reaction intermediates during CO2 electroreduction via first-principles molecular dynamics modeling. This reaction is timely and has, over the last few years, served as the playground for advanced atomistic modeling of electrocatalysis (49).

The general lack of understanding is due to the inherent complexity of the electrified interface and its characterization. The characterization is difficult since most metal–liquid interfaces are amorphous. Therefore, no long-range ordering can be detected. Experimentally, the characterizations heavily rely on spectroscopy that provides average molecular orientations [infrared (IR) and Raman] or elemental composition and oxidation states (X-ray photoelectron, X-ray absorption near-edge, etc.) (1012). Atomically resolved structures can be obtained only for rare, crystalline interfaces such as pyridine on gold single-crystal surfaces via scanning tunneling microscopy imaging (13, 14). Theoretically, the simulations of electrochemical interfaces are challenging for two reasons. The first challenge originates from the structure and dynamics of the interface; that is, its size and the relevant timescales. Just like for experiments, the amorphous nature of the interface means that, when working with periodic boundary conditions to well describe the metallic nature of the electrode and the liquid nature of the electrolyte, large systems need to be simulated to avoid spurious periodicity and thus simulation-induced crystallinity. Furthermore, the electrode surface might reconstruct in reaction conditions (15). Even in the absence of reconstructions, the dynamics at the interface tend to be orders of magnitude slower than in solution, so the necessary simulations to reach equilibrium are computationally expensive (1618).

The second challenge is related to the presence of an electrochemical potential. To accurately describe chemical-bond breaking, density functional theory (DFT) computations have to be performed. However, in DFT, the positions of the electrons are optimized and cannot be chosen at will. In practice, simulating the effect of an electrochemical potential goes along with tuning the number of electrons at the metal surface, neutralized with a countercharge of either atomistic or continuous nature (19, 20). Although the introduction of anions/cations corresponds to the operando experimental conditions, the sampling of the explicit counterion distribution becomes very challenging. During a given simulation, the number of counterions is usually kept constant, resulting in a fluctuating electrochemical potential. Grand canonical simulations, which keep the potential constant while varying the number of counterions, are technically feasible but would require 1 to 2 orders more time to obtain equilibrated results. On top of that, usual DFT functionals lead to self-interaction errors and associated incorrect electron localization (21). The field of electrocatalysis modeling is thus at a critical point, where simple approximations lack accuracy, but more realistic modeling is computationally very expensive. A full description from first principles of the structure, energetics, and dynamics of the electrochemical interface is, therefore, extremely challenging, if not inaccessible, with today’s methods.

The overarching idea of Cheng et al. (3) in PNAS is to combine experimental and theoretical IR spectroscopy to identify the nature of key reaction intermediates for CO2 electroreduction (Fig. 1). This relies on the fact that, in general, the accuracy of vibrational spectra from DFT is superior to the accuracy of thermodynamic and kinetic parameters. Hence, assigning the experimental spectra by theoretical computations can provide insight into the species present on the electrode. Such insight is critical for catalyst design that aims at reducing overpotentials (i.e., energetic losses) and at obtaining high yield and selectivity in the targeted chemical product (e.g., ethylene).

Fig. 1.

Fig. 1.

Schematics of the identification procedure of surface intermediates involved in an electrocatalytic reaction by matching experimental and simulated spectra, taking into account the dynamics of the solvent and electrolyte and the applied potential.

In electrocatalysis, the reaction occurrs at the interface between the electrode and the electrolyte. This interface is classically described by the double-layer theories from Helmholtz, Gouy, Chapman, and others. These models treat the solvent and electrolyte in an averaged manner, neglecting most atomistic effects such as finite size and preferred molecular orientations. This contrasts with the atomistic models of metal surface in contact with water, which demonstrate a partial immobilization of the solvent at the electrode interface and a high degree of structuring. This interfacial structuring has, necessarily, an influence on adsorbate geometries, energies, and vibrational spectra beyond the electric field effect due to the electrochemical potential (22).

Cheng et al. (3) adopt the confident strategy to rely on explicit, brute-force, atomistic calculations of the electrode–electrolyte interface: The simulations are initialized by long molecular dynamics simulations with an approximate, but much faster, method relying on a parametrized force field. The authors then switch to the DFT description for a simulation that is 100 times shorter, from which they extract the vibrational spectrum. For the local configuration, such a short simulation has previously been shown to be sufficient for retrieving thermodynamic functions and vibrational spectra for liquids. This combination of two levels of theory is highly elegant and close to the best compromise achievable today between the opposing needs of extensive configuration sampling and high accuracy in energies. Future developments of the methods (and computers) will certainly allow alleviation of some unavoidable present shortcomings. Notably, the approach is currently limited to rather small systems; in the present case, only 48 water molecules are included. For bulk water (i.e., where there are no interfaces), 64 water molecules were found necessary to converge the average structure of the liquid (23). Hence, the water structure and properties might deviate somewhat from the fully converged result. Another question relates to the water structure at the interface which might require large supercells. However, the major limitation that needs to be overcome is efficiently averaging over diverse adsorbate–electrolyte arrangements as a function of the potential and electrolyte, since a single local configuration is unlikely to be fully representative. A further bottleneck to be overcome is the parametrization of the efficient, approximate method used for system equilibration.

In PNAS, Cheng et al. bring key insight to the characterization of reaction intermediates during CO2 electroreduction via first-principles molecular dynamics modeling.

Indeed, this method would need to be generalized to other metals, alloys, materials, and electrolytes to cover the whole range of electrified solid–liquid interfaces that could benefit from the application of the strategy of Cheng et al. to elucidate the species and processes at the electrode–electrolyte interface. Last, but not least, the accuracy of DFT for systems with separated charges (electrode/counterions) needs to be improved to confidently simulate the charge distribution at these interfaces.

With such a general method at hand, we could expect major breakthroughs in the atomistic understanding and rational design of electrified interfaces in various domains, such as the development of the next generation of Li-, Na-, or Mg-based batteries with a higher energy and power density. Of course, the domain of super- and pseudocapacitors (24), in which electrical energy is stored at high rates, would also greatly benefit from an operando view on the species and reactions present at the electrode. Similarly, organic electronics could be better described if the influence of the applied voltage and the surrounding electrolyte were included. On a more industrial level, these methods would also be ideally suited to study electroplating and corrosion (25), which is very poorly understood and, despite its economic importance (corrosion generates costs of ∼3% of the gross domestic product) (26), underrepresented in fundamental research. Lastly, the characterization of relevant reaction intermediates during electrocatalytic reactions might accelerate catalyst design in diverse areas of electrolysis and fuel cells, including the production of hydrogen over (nonnoble) metals from water reduction and biomass oxidation; the improvement in the still incompletely understood oxygen reduction and evolution reaction; the development of efficient nitrogen reduction catalysts that would allow the decentralization of ammonia production; and, of course, the CO2 electroreduction investigated by Cheng et al. (3) that has the potential to sustainably close the carbon cycle by converting the greenhouse gas CO2 into carbon building blocks that, one day, could replace fossil resources as the basis of chemical industry.

Acknowledgments

Z.-Y.W. and P.S. are supported by the Center for Synthetic Control Across Length-scales for Advancing Rechargeables, an Energy Frontier Research Center funded by the US Department of Energy, Office of Science Basic Energy Sciences program under Award DE-SC0019381. S.N.S. is supported by Project MuSiC (Grant ANR-14-CE06-0030) of the French National Research Agency.

Footnotes

The authors declare no conflict of interest.

See companion article on page 7718.

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