Tao
Cheng
a,
William A
Goddard
III
*a,
Qi
An
a,
Hai
Xiao
a,
Boris
Merinov
a and
Sergey
Morozov
b
aMaterials and Process Simulation Center (MC139-74), California Institute of Technology, Pasadena, California 91125, USA. E-mail: tcheng@caltech.edu; anqi@caltech.edu; xiao@caltech.edu; merinov@wag.caltech.edu; wag@wag.caltech.edu
bSouth Ural State University Lenina, 76, Chelyabinsk, Chelyabinsk Oblast, Russia. E-mail: morozov72@gmail.com
First published on 21st December 2016
The sluggish oxygen reduction reaction (ORR) is a major impediment to the economic use of hydrogen fuel cells in transportation. In this work, we report the full ORR reaction mechanism for Pt(111) based on Quantum Mechanics (QM) based Reactive metadynamics (RμD) simulations including explicit water to obtain free energy reaction barriers at 298 K. The lowest energy pathway for 4 e− water formation is: first, *OOH formation; second, *OOH reduction to H2O and O*; third, O* hydrolysis using surface water to produce two *OH and finally *OH hydration to water. Water formation is the rate-determining step (RDS) for potentials above 0.87 Volt, the normal operating range. Considering the Eley–Rideal (ER) mechanism involving protons from the solvent, we predict the free energy reaction barrier at 298 K for water formation to be 0.25 eV for an external potential below U = 0.87 V and 0.41 eV at U = 1.23 V, in good agreement with experimental values of 0.22 eV and 0.44 eV, respectively. With the mechanism now fully understood, we can use this now validated methodology to examine the changes upon alloying and surface modifications to increase the rate by reducing the barrier for water formation.
The slow electrocatalysis of the oxygen reduction reaction (ORR) looms as the central issue. Currently, the best ORR catalysts are based on Pt or Pt alloys, but after years of research, the performance remains inadequate, requiring far too much Pt to be economical and requiring a considerable overpotential, η ∼0.3 V.9–12 For example, the DOE targets are As = 0.7 mA cm−2 (2015) and Am = 0.44 A per mgpt (2017)5 whereas the best commercial Pt/C catalysts have a specific activity As = 0.127 mA cm−2 and a mass activity Am = 0.096 A per mgpt at 0.9 V under working conditions.13
Catalysis performance has been improved significantly by nanoscale designs including alloying of Pt with such metals as Ni or Co.14 Other promising reports15–19 include a Mo–Pt3Ni/C catalyst claimed to exceed DOE targets.13 However, many suggested systems have problems with performance degradation (e.g., dealloying).4,20
We consider that catalyst development is hampered by an incomplete understanding of the reaction mechanism underlying the ORR. Several general guidelines based on theoretical insights and experimental observations have been proposed,21 but there is no consensus of the controlling factors underlying ORR.
The ORR reaction involves three basic steps:22,23
(1) Breaking the O–O bond, which may be
(a) Dissociative
*O2 → O* + O* | (1a) |
(b) Associatively dissociative (Jacob and Goddard24)
*O2 + H+ + e− → *OOH | (1b) |
*OOH → *OH + O* | (1c) |
(c) Associatively reductive (a new mechanism we report here)
*O2 + H+ + e− → *OOH | (1b) |
*OOH + H+ + e− → H2O(aq) + O* | (1c′) |
(2) Conversion of O* to *OH, which may occur by
(a) Electrochemical reduction
O* + H+ + e− → *OH | (2a) |
(b) Langmuir–Hinshelwood (LH) hydrolysis using surface H2O* (Sha, Goddard, and coworkers25)
O* + H2O* → *OH + *OH | (2b) |
(3) Conversion of OH* to H2O
*OH + H+ + e− → H2O | (3) |
These various reaction mechanisms lead to several possible rate-determining steps (RDS).
In the work of Gómez-Marín and Feliu,26 kinetic analysis of the cyclic voltammetry profile showed that the cathodic current depends to first-order on the O2 concentration in agreement with rotating disk electrode (RDE) experiments.27 The linearity of the Koutecky–Levich plot was considered as evidence that the RDS is the first electron transfer step. Therefore, either *O2− formation in base solution28 or hydroperoxyl (*OOH) formation (1b) in acid solution was proposed to be the RDS.29–31 However, recent kinetics simulations show that this first order O2 dependency can be explained by slow adsorption of O2 into the solution, leading to a low O2 concentration and slow solvent reorganization at the interface.32 Therefore, the first electron transfer step need not be the RDS, even though the overall reaction rate is of order one in O2. This opens up the possibilities of other elementary reaction steps as the RDS.
For example, the water formation step (3) has also been widely proposed as the RDS based on experiments showing significant hydroxyl concentration (*OH) under working conditions,33 indicating that either the *OH species is an ORR intermediate or the reactant.34–36 This was supported by QM calculations showing that adsorbed oxygen and *OH are stable intermediates at potentials close to equilibrium.21 Furthermore, DFT calculations with explicit consideration of the reconstructed surface indicated that *OH removal from the surface determines the overpotential.37
Nevertheless, reaction kinetics under real operating conditions may be much more complex. Very possibly, ORR kinetics is not determined solely by a single factor, but with multiple RDS coexisting. Indeed, a recent experiment demonstrated that under operating conditions two phases of *OH coexist: hydrated *OH and non-hydrated *OH. Moreover, the possible coexistence of two sets of kinetics has been demonstrated by DFT calculations: H2O formation could be the RDS in the hydrated pathway, while *OOH formation is the RDS in the non-hydrated pathway.38
Other possible ORR reaction mechanisms have been discussed in previous studies.25,26 Such controversies in the ORR reaction mechanism could be resolved by determining the reaction intermediates experimentally. However, in situ experimental methods have not been able to detect oxygenated adsorbed species reliably. Nano-electronic strategies are in development for in situ electrochemical surface studies with high surface sensitivity and surface specificity, which might eventually extend the understanding of the nature of catalysis interface and ORR reaction mechanism.39
Quantum mechanics (QM) calculations can provide critical atomistic mechanistic insight about ORR reactions. However, previous studies have all been deficient in including the effect of the solvent fully. Early calculations ignored the solvent, while later ones used implicit solvation methods sometimes with a few explicit solvent molecules.7,24,25,40 Explicit simulation of solvent41–44 becomes more popular attribute to the upgrade in hardware and software. These various solvation models have led to a range of inconsistent results. For example, the predicted free energy barriers for O2 dissociation range from 0.0 eV to 0.7 eV, depending on the solvation model.23,25,40 Consequently, we concluded that it is essential to use ∼5 layers of explicit waters to describe reactions at the catalyst–solvent interface properly. Indeed, because the extrapolated experimental apparent activation energy at 0.8 V is only 0.2 eV to 0.6 eV,45–48 the QM barriers must be accurate to 0.1 to 0.2 eV to pinpoint the key steps.
Here we simulate the water/Pt(111) interface using 48 explicit water molecules on a 4 × 4 × 3 Pt(111) surface slab with area 1.08 nm2. This leads to 5 layers of explicit water with a thickness of 1.5 nm, as shown in Fig. 1A. To equilibrate the waters interacting with the interface, we need to carry out ∼2 ns of molecular dynamics at 298 K NVT, but Reactive Molecular Dynamics (RMD) using Quantum Mechanics (QM) forces (termed AIMD) is practical on this system for only 10 ps or so. Thus to fully equilibrate the water–Pt interface, we carried out 2 ns of RMD simulations using the ReaxFF reactive force field49 for Pt and H2O. Starting from this well-equilibrated interface, we made 10 ps of AIMD simulation at 298 K using metadynamics to calculate the free energy barriers for each of numerous possible reaction steps. We consider that this model of QM with explicit treatment of the water dynamics at operating temperature provides a reliable description of the reaction kinetics.
Fig. 1A shows the density profile of the water layers, with three clear peaks near the surface. The first peak at ∼3 Å from the Pt surface corresponds to the first contact layer of water, consisting of 11 water molecules with one chemisorbed O2 leading to a surface coverage close to the 2/3 ML suggested by the bilayer water model.50 This first contact layer of water contains an integrated hydrogen bond network (shown in Fig. 1B), but with irregular and fluctuating five member rings and six member rings rather than the perfect six member rings from energy minimized structures.51 The presence of O2 in this first layer slightly distorts the hydrogen bond (HB) network, so that this O2 forms one HB with a water molecule in the second layer. The density of the first layer is about 2.0 g cm−3, twice that of bulk water. The second layer leads to a significant peak between 0.6 and 0.7 nm, slightly longer than the normal 0.3 nm HB distance away from the first layer. The third layer is less structured but distinguishable; the protonated water prefers this layer. These three layers have a total thickness of ∼1 nm, providing the most relevant regions for surface reactions. For the next ∼0.2 nm (1.0 nm to 1.2 nm) the density is ∼1.0 g cm−3, the bulk value of water at 298 K. Finally, at 1.5 nm we reach the vapor/liquid interface which is ∼0.2 nm thick. No evaporated water was observed in the RMD simulations. These results demonstrate that a 1.5 nm thick water layer is sufficient to simulate the interface reactions (Table 1).
Step | Reactions | Reaction equations | ΔG‡AIMD (eV) | ΔG‡ (eV) |
---|---|---|---|---|
1a | *O2 dissociation | *O2 → O* + O* | 0.40 (3) | |
1b | *O2 association (LH) | *O2 + H* → *OOH | 0.22 (7) | |
1c | *OOH dissociation | *OOH → O* + OH* | 0.38 (8) | |
1c′ | *OOH reduction (LH) | *OOH + H* → H2O + O* | 0.29 (7) | |
1c′ | *OOH reduction (ER@0.6V) | *OOH + H+ + e− → H2O + O* | 0.14 (6) | |
1c′′ | HOOH formation (LH) | *OOH + H* → HOOH | 0.48 (5) | |
2c | O* hydrolysis (LH) | O* + H2O* → *OH + *OH | 0.25 (6) | |
3a | Water formation (LH) | *OH + H* → H2O | 0.54 (8) | |
3b | Water formation (ER@0.6 V) | *OH + H+ + e− → H2O | 0.16 (7) | 0.12 (13) |
3b | Water formation (ER@1.1 V) | *OH + H+ + e− → H2O | 0.39 (6) | 0.35 (12) |
This pure water/Pt interface corresponds to the catalysis surface in the diffusion region of the ORR reactions (0.3 V to 0.6 V). For more positive potentials, *OH may accumulate on the surface, so that under working condition (0.8 V to 0.9 V) the surface layer may be partially dissociated, including both water and hydroxyl (*OH). However, kinetic analyses conclude that dissociated surface H2O has only a slight negative electronic effect on ORR kinetics for the case of a weak acid compared with the pure water/Pt surface.32 This suggests that the reaction mechanisms are similar even if the surface has dissociated water. Therefore, the ORR reaction mechanism derived here based on the water/Pt surface should also apply to the real surface at 0.8 to 0.9 V.
We carried out metadynamics QM simulations at 298 K to predict the reaction free energy barriers for all plausible ORR elementary steps in reactions (1), (2), and (3). The Langmuir–Hinshelwood (LH) model has been used in previous calculations that did not contain an explicit solvent to simulate the electrochemical reaction, in which case H* is related to H+ + e− by H+ + e− → H*.7,20
(1a+2c) |
(1b−2c) |
This high reactivity of surface water, H2O*, has not previously been suggested (we discovered it first in unpublished ReaxFF reaction simulations). The reason why surface H2O is so reactive is that the binding energy of H2O to Pt is only 0.2 eV insolvent, while *OH binds by 1.0 eV (referenced to H2 + H2O), making the OH bond of surface water 0.8 eV more active than normal H2O.
The second hydrolysis step was observed during the timescale of the O2 dissociation step, suggesting that some of the reaction energy of the 1st step may help drive this second step, rather than being dissipated. The small O* hydrolysis barrier of 0.25 eV (Fig. S2, ESI†) indicates that surface water may play a major role in ORR reactions and it shows that non-electrochemical steps may accelerate an overall electrochemical reaction, providing a potentially useful design principle for electrocatalytic processes.
The presence of *OOH also leads to the possibility of HOOH formation (1c′′), but we find ΔG‡ = 0.48 eV, which is the largest barrier among the three branches from *OOH. This indicates that HOOH formation is unfavorable on Pt(111), consistent with the lack of HOOH formation observed experimentally for Pt(111) under ORR conditions.52
*OH + H+ + e− → H2O(aq) | (3a) |
Summarizing, the free energy barriers for the various reduction steps are:
(1) ΔG‡ = 0.22 eV for O2 association (1b);
(2) ΔG‡ = 0.29 eV for *OOH reduction (1c′) and 0.25 eV for O* hydration by surface water (2b);
(3) ΔG‡ = 0.54 eV for water formation (3a).
Therefore, the reaction mechanism describing the minimal energy kinetic pathway is as follows:
(4) |
These free energy barriers were identified with normal finite temperature QM RMD in which the number of electrons is fixed. To convert these values to constant applied potential conditions of the experiments, we used the post-QM correction method proposed by Chan and Nørskov,53 but we replace the charge (which is ambiguous in plane wave DFT calculations) with capacitance. Details for calculating these corrections to the various reaction steps are tabulated in the ESI† (Table S1).
For QM RMD simulations of reactions involving H3O+ + e−, we replace one of the 48 H2O with H3O, which becomes H3O+ with an increased electron density on the Pt electrode. The extra electron increases the Pt work function (WF) leading to U = 0.6 V. Because the number of electrons is constant as the reaction path is sampled in metadynamics, the WF changes along the reaction coordinate. These potential changes can influence the rate of water formation since water formation is thermodynamically favorable at 0.6 V, but unfavorable at 1.0 V. Therefore, we used collective variables that constrain both of the two OH bond lengths to force water formation. The calculated free energies were corrected back to 0.6 V based on the calculated changes going through the transition state.
The inclusion of Pt–O in the CV makes it necessary to ensure that the water product detaches from the surface site. The two-dimensional free energy surface calculated with this CV is shown in Fig. 3A. At 0.6 V, the free energy barrier from the QM RMD is 0.16 eV, which becomes 0.12 eV after correction for constant potential. The reaction pathway for proton transfer is shown in Fig. 4. In these simulations, we found that the proton forms an H5O2+ complex involving one water molecule from the first layer and a 2nd water molecule from the 2nd layer. Three intermediate water molecules participate in bridging H5O2+ and *OH via a Grotthuss HB proton tunneling network as shown in Fig. 4.
The reaction barriers for constant potential conditions depend on the magnitude of the potential. Experimentally, this dependence can be characterized by the symmetry factor (β), which is related to the fraction of the charge transfer that occurs in the transition state. Experimentally, β is derived from the Tafel slope by applying a series of potentials. In our simulations, we control the potential by adding ions into the system. For example, introducing one Cl into the system increases the potential from 0.6 to 1.1 V, because Cl extracts an e− from the electrode to form Cl−, thereby increasing the WF to a more positive potential. The two-dimensional free energy surface for water formation (ER) calculated at 1.1 V is shown in Fig. 3B. At this voltage, water formation is already energetically unfavorable. Therefore, the free energy is uphill from *OH to water. The free energy barrier predicted from the metadynamics is 0.39 eV, which becomes is 0.35 eV after correcting to a constant potential.
For U > 0.3 V all reaction barriers involving H* will be lower for ER than for LH. For example, the ER model leads to a free energy barrier for *OOH reduction that is 0.15 eV lower than for LH (Fig. S5 and S6, ESI†). Because all steps in eqn (4) involve H*, the reaction mechanism based on LH free energies still applies to the ER model, by simply changing H* to H+ + e−.
Our predicted ER barriers at 0.6 and 1.1 V leads to , which we use to predict the free energy barrier for ER water formation between 0.35 V to 1.23 V, as shown in Fig. 5 (the lower limit is taken as 0.1 eV, the diffusion barrier for proton transfer). Thus we predict that
Fig. 5 Predicted activation energies (free energy barriers, ΔG‡ in eV) for the rate determining steps from QM RμD calculations at various applied potentials, compared to experimental data (enthalpy, ΔH‡ in eV). The theory suggests that ΔG‡ = 0.25 eV for O* hydrolysis (solid green line) is rate determining below 0.87 V, while water formation via ER (solid black line) dominates at higher potential. The potential dependence of water formation (ER) was derived from the simulations at 0.6 V leading to ΔG‡ = 0.12 eV and at 1.1 V leading to ΔG‡ = 0.35 eV, leading to a slope of 0.46. The reaction barrier for proton transfer (∼0.1 eV) is taken as the lower limit for this step. The experimental data Exp 2 (red, Paulus et al. 2002)48 and Exp 3 (blue, Grgur et al. 1997),46 were determined by fitting to the Arrhenius equation the observed exchange current density (from the Tafel slope) over the temperature range 298–333 K. The results in Exp 1 (purple, Beattie et al. 1999)45 may involve organic impurities from the Nafion solution. Note that the LH barrier of 0.29 eV for H* + *OOH reduction is reduced by the ER mechanism to below the 0.25 eV for O* hydrolysis for U > 0. |
• for U < 0.87, ΔG‡ = 0.25 eV (O* hydrolysis) a constant
• for U > 0.87. ΔG‡ is determined by ER production of H2O, which increases linearly to 0.41 eV at 1.23 V.
These results are in excellent agreement with experimental values from Markovic and coworkers46,48 (based on fitting to the Arrhenius equation the exchange current density from the Tafel slope over the temperature range of 298–333 K).
• ΔG‡ = 0.20 to 0.25 eV at U = 0.82 to 0.93 eV and
• ΔG‡ = 0.44 eV at 1.23 V.
Other experimental studies using a Nafion electrolyte45 obtained ΔG‡ = 0.4 and 0.6 eV at U = 0.8. This significantly larger activation energy may be attributed to organic impurities from the Nafion solution, as explained by the authors.45
Summarizing, we used QM based Reactive Molecular Dynamics at 298 K to predict the free energy barriers for ORR reactions on Pt(111) while including five layers of explicit water to simulate the water/Pt(111) interface. We corrected for the effect of the applied potential on the work function change during charge transfer for the various reaction steps to convert the constant electron QM results to constant potential QM. We find that the RDS has ΔG‡ = 0.25 eV for U < 0.87, but it increases linearly to 0.41 at 1.23 V, in excellent agreement with experiment. An important discovery is that surface H2O* plays an essential role in donating the H to various reaction steps, a non-electrochemical potential independent reaction (as suggested by Sha, Goddard, and coworkers).25
With a validated mechanism in hand and a validated QM methodology, we can now consider how to modify these various steps can be by alloying, surface modification, changes in the electrolyte, etc. to further optimize the rates and overpotentials. Thus if the predicted potential dependent barrier of 0.41 eV at 1.23 V could be brought down to the potential independent value of 0.25, the rate for ORR would increase by a factor of 600 at 298 K, while allowing an operating over potential close to zero. This would most dramatically change the economics for fuel cells for transportation and utilize the chemical energy from solar fuel production.
Footnote |
† Electronic supplementary information (ESI) available: Simulation methods, Fig. S1–S7, Table S1 and ref. 49–59. See DOI: 10.1039/c6cp08055c |
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