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			<titleStmt><title level='a'>What Is the Rate-Limiting Step of Oxygen Reduction Reaction on Fe–N–C Catalysts?</title></titleStmt>
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				<publisher>ACS</publisher>
				<date>11/22/2023</date>
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				<bibl> 
					<idno type="par_id">10562916</idno>
					<idno type="doi">10.1021/jacs.3c09193</idno>
					<title level='j'>Journal of the American Chemical Society</title>
<idno>0002-7863</idno>
<biblScope unit="volume">145</biblScope>
<biblScope unit="issue">46</biblScope>					

					<author>Saerom Yu</author><author>Zachary Levell</author><author>Zhou Jiang</author><author>Xunhua Zhao</author><author>Yuanyue Liu</author>
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			<abstract><ab><![CDATA[Oxygen reduction reaction (ORR) is essential to various renewable energy technologies. An important catalyst for ORR is single iron atoms embedded in nitrogendoped graphene (Fe-N-C). However, the rate-limiting step of the ORR on Fe-N-C is unknown, significantly impeding understanding and improvement. Here, we report the activation energies of all of the steps, calculated by ab initio molecular dynamics simulations under constant electrode potential. In contrast to the common belief that a hydrogenation step limits the reaction rate, we find that the rate-limiting step is oxygen molecule replacing adsorbed water on Fe. This occurs through concerted motion of H 2 O desorption and O 2 adsorption, without leaving the site bare. Interestingly, despite being an apparent "thermal" process that is often considered to be potential-independent, the barrier reduces with the electrode potential. This can be explained by stronger Fe-O 2 binding and weaker Fe-H 2 O binding at a lower potential, due to O 2 gaining electrons and H 2 O donating electrons to the catalyst. Our study offers new insights into the ORR on Fe-N-C and highlights the importance of kinetic studies in heterogeneous electrochemistry.]]></ab></abstract>
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<div xmlns="http://www.tei-c.org/ns/1.0"><head>&#9632; INTRODUCTION</head><p>Oxygen reduction reaction (ORR) is essential to a variety of renewable energy technologies such as fuel cells and metal-air batteries. Platinum is the best-performing catalyst for ORR. However, it suffers from high cost, which impedes its commercial use. <ref type="bibr">[1]</ref><ref type="bibr">[2]</ref><ref type="bibr">[3]</ref><ref type="bibr">[4]</ref> To overcome this obstacle, tremendous research efforts have been dedicated to finding cost-effective alternative catalysts to Pt. <ref type="bibr">[5]</ref><ref type="bibr">[6]</ref><ref type="bibr">[7]</ref><ref type="bibr">[8]</ref><ref type="bibr">[9]</ref><ref type="bibr">[10]</ref> One of the most promising candidates is single iron atoms embedded in nitrogen-doped graphene (Fe-N-C), which is often used in acidic conditions. <ref type="bibr">[11]</ref><ref type="bibr">[12]</ref><ref type="bibr">[13]</ref><ref type="bibr">[14]</ref><ref type="bibr">[15]</ref><ref type="bibr">[16]</ref><ref type="bibr">[17]</ref><ref type="bibr">[18]</ref> Despite extensive studies on this catalyst, it is still unknown what step limits the ORR rate on Fe-N-C. The lack of this critical information significantly limits catalyst development.</p><p>A commonly suggested pathway for ORR on Fe-N-C has the following steps (Figure <ref type="figure">1a</ref>): * + O 2 &#8594; *OO, *OO + H + + e -&#8594; *OOH, *OOH + H + + e -&#8594; *O + H 2 O, *O + H + + e - &#8594; *OH, *OH + H + + e -&#8594; * + H 2 O. Experimental determination of the rate-limiting step is challenging. On the other hand, density functional theory (DFT) offers a means to calculate the reaction energetics, including activation energies, and thus in principle can answer the question about the rateliming step. However, directly calculating activation energies of heterogeneous electrochemistry is difficult due to the complexity of the system, which requires careful treatments of the effects of solvation and electrode potential. <ref type="bibr">[19]</ref><ref type="bibr">[20]</ref><ref type="bibr">[21]</ref><ref type="bibr">[22]</ref><ref type="bibr">[23]</ref><ref type="bibr">[24]</ref><ref type="bibr">[25]</ref><ref type="bibr">[26]</ref><ref type="bibr">[27]</ref><ref type="bibr">[28]</ref><ref type="bibr">[29]</ref> Therefore, most computational studies calculate the thermodynamics of each step and use it to infer the kinetics, based on the assumption that the most thermodynamically uphill (or the least downhill) step has the highest activation energy. Those papers typically show that either the *OO + H + + e -&#8594; *OOH or the *OH + H + + e -&#8594; * + H 2 O step is the thermodynamically limiting step. <ref type="bibr">[29]</ref><ref type="bibr">[30]</ref><ref type="bibr">[31]</ref><ref type="bibr">[32]</ref><ref type="bibr">[33]</ref><ref type="bibr">[34]</ref><ref type="bibr">[35]</ref><ref type="bibr">[36]</ref> Both steps involve hydrogenation of the adsorbate. However, thermodynamics does not necessarily correlate with kinetics. Hence, the information on activation energies is indispensable to identify the rate-limiting step.</p><p>To address this critical need, here we calculate the activation energies of ORR steps on Fe-N-C, using a recently developed model: "constant-potential hybrid solvation-dynamic model" (CP-HS-DM). <ref type="bibr">20</ref> This model enables effective simulation of electrochemical kinetics at the solid-water interface, by directly including the explicit solvation and electrode potential into the model. The results reveal a different reaction mechanism from the commonly believed one: instead of the hydrogenation step, the rate-limiting step is the replacement of the preadsorbed H 2 O molecule by the O 2 molecule on the Fe atom; despite being an apparent "thermal" process, the activation energy of this step decreases with decreasing electrode potential, due to the enhanced Fe-O 2 binding while weakened Fe-OH 2 binding at a lower potential. Our work provides new insights into the ORR and Fe-N-C catalytic mechanisms and highlights the significance of kinetic information that is generally lacking in the current study of heterogeneous electrocatalysis.</p></div>
<div xmlns="http://www.tei-c.org/ns/1.0"><head>&#9632; METHODS</head><p>The CP-HS-DM <ref type="bibr">20</ref> is one realization of the constant-potential ab initio molecular dynamics (cp-AIMD) with explicit water. The supercell contains a thin film of explicit water molecules on top of the catalyst. The remaining space is filled with implicit solution modeled as a continuous dielectric medium with point ionic charges. This implicit solution serves to balance the extra charges in the explicit region and introduces a region with a flat electrostatic potential profile that can be used to extract the relative electrode potential. The structure is evolved using AIMD with an enhanced sampling technique, and the electron number changes under potentiostat.</p><p>In this work, we perform CP-HS-DM simulation using Vienna Ab initio Simulation Package (VASP), <ref type="bibr">37,</ref><ref type="bibr">38</ref> leveraging the VASPsol <ref type="bibr">39,</ref><ref type="bibr">40</ref> implicit solvation model. We have implemented the cp-AIMD method as a patch to the VASP code (the patch file is available to the readers upon reasonable request). To compute the free energy profile, we employed thermodynamic integration. Specifically, we first run slowgrowth simulation <ref type="bibr">41</ref> to obtain a preliminary profile and then run blue moon simulation <ref type="bibr">42,</ref><ref type="bibr">43</ref> to obtain a more accurate one. To model the acidic conditions, we add one H to the explicit water molecules. The details of our calculations can be found in the Supporting Information (SI).</p></div>
<div xmlns="http://www.tei-c.org/ns/1.0"><head>&#9632; RESULTS AND DISCUSSION</head><p>Our study first focuses on U = 0.5 V vs SHE because it is within the typical range of working potentials. <ref type="bibr">12,</ref><ref type="bibr">44,</ref><ref type="bibr">45</ref> Our cp-AIMD simulations show that when Fe-N-C is in contact with water, a H 2 O molecule is adsorbed onto the Fe site. When we intentionally desorb H 2 O via slow growth, another H 2 O molecule will occupy the Fe site (see SI Section 3). This result indicates that before ORR, the Fe site is already occupied by a H 2 O molecule, consistent with a recent paper. <ref type="bibr">29</ref> Then how does the adsorption of O 2 take place? We find that the adsorption of O 2 occurs concertedly with H 2 O desorption. As shown in Figure <ref type="figure">1c</ref> H 2 O step as an example. In this step, as the *O-OH bond breaks, the proton attacks the generated OH to form H 2 O.</p><p>During this process, the system gradually acquires excessive electron concentrating on the higher O, which attracts the proton closer and facilitates the H 2 O formation. Consequently, the barrier is low, only 0.15 eV. It is worth noting that this change in electron number cannot be observed in the conventional constant-charge simulation, thereby necessitating the use of the constant-potential method as we employed here. Additionally, the Fe-N-C surface exhibits a positive charge under 0.5 V. This is because its potential of zero charge (PZC) is lower than 0.5 V. In other words, at a charge-neutral state,  </p></div>
<div xmlns="http://www.tei-c.org/ns/1.0"><head>Journal of the American Chemical Society</head><p>the Fermi level of Fe-N-C is higher than that of the electrode. To align the Fermi levels, Fe-N-C has to lose electrons, thereby acquiring a positive charge. Another interesting finding is that at the initial state, the proton is located closer to the higher O than the lower O in the *O-OH on Fe-N-C. This contrasts the Co-N-C catalyst, where the proton prefers the lower O. <ref type="bibr">20</ref> Therefore, after the proton attacks the closer O, Fe-N-C will generate H 2 O, whereas Co-N-C will produce H 2 O 2 . This explains the difference in ORR selectivity observed for these two catalysts. To check if our conclusion still holds at a lower potential, we also study ORR at U = 0.1 V vs SHE. This potential is chosen because it is not too low to be unrealistic but low enough to show a significant difference. <ref type="bibr">12,</ref><ref type="bibr">44,</ref><ref type="bibr">45</ref> As shown in Figure <ref type="figure">3</ref>, we find that all electrochemical steps become barrierless while the *H 2 O + O 2 &#8594; *O 2 + H 2 O step still has a barrier of 0.26 eV. Therefore, the rate-limiting step is still</p><p>It is interesting to see that the activation energy of *H 2 O + O 2 &#8594; *O 2 + H 2 O noticeably decreases when the potential is decreased (Figure <ref type="figure">3</ref>). This challenges the conventional view that it is a thermal step (as it does not explicitly involve electron(s)) and should be potential-independent. To understand the origin, we calculate the adsorption energies of O 2 and H 2 O on Fe-N-C under different potentials (without solvent molecules for simplicity). As shown in Figure <ref type="figure">4a</ref>, decreasing the potential enhances the O 2 adsorption while weakening the H 2 O adsorption. Therefore, the lower barrier at the lower potential can be explained by the stronger driving force provided by the enhanced binding with O 2 and the weakened binding with H 2 O.</p><p>The potential-induced change in the binding strength can be attributed to different surface charges under different potentials. Our calculations (without solvent for simplicity) show that the bare Fe-N-C acquires &#8764;1 electron as the potential decreases from 0.5 to 0.1 V. This large change in the surface charge results in a significant change in the electronic state occupation, thereby altering the chemical reactivity of Fe-N-C. <ref type="bibr">21</ref> But why do O 2 and H 2 O have opposite responses to the surface charge? This can be explained by the opposite directions of charge transfer. We find that upon adsorption, O 2 gains electrons from Fe-N-C while H 2 O donates electrons (see Figure <ref type="figure">4b</ref>). Increasing the electronic charges on Fe-N-C will enhance the electron transfer to the adsorbate while suppressing the back-transfer. Therefore, reducing the potential strengthens the binding with O 2 while weakening that with H 2 O. This mechanism suggests that to design more active sites for ORR, one may target those that are more negatively charged (under the same electrode potential), because they can have lower activation energies for the rate-</p><p>The charge transfer theory also explains the potential dependence of the adsorption energies of other intermediates (*OOH, *O, and *OH). As shown in Figure <ref type="figure">S9a</ref>, the potential decrease enhances their bindings with the catalyst. This can be attributed to the fact that they all gain electrons from the catalyst (Figure <ref type="figure">S9b</ref>).</p><p>Although our focus here is on the acidic conditions, as Fe-N-C is mainly used in proton exchange member fuel cells, it is worth considering other pH conditions. For the same RHE potential, the SHE potentials are lower under alkaline conditions than under acid conditions. In other words, the catalyst surface is more negatively charged under alkaline conditions. According to our findings, a more negatively charged site should have a lower barrier for the *H 2 O + O 2 &#8594; *O 2 + H 2 O step. On the other hand, the proton source is a water molecule under alkaline conditions and it is more difficult to donate protons than H 3 O + . Therefore, compared with acidic conditions, we anticipate that in alkaline conditions the *H 2 O + O 2 &#8594; *O 2 + H 2 O step will become easier, whereas the hydrogenation steps will become more difficult.</p></div>
<div xmlns="http://www.tei-c.org/ns/1.0"><head>&#9632; CONCLUSIONS</head><p>In this study, we employed an advanced first-principles model to reveal the rate-limiting step of ORR on Fe-N-C. We discovered a new mechanism that O 2 replaces the preadsorbed  H 2 O on Fe through a concerted motion without leaving the Fe site bare. This step was found to have the largest activation energy among the ORR steps. The barrier of this step counterintuitively lowers with decreasing electrode potential, due to the stronger O 2 adsorption and weaker H 2 O adsorption when the surface carries more electronic charges. This can be further explained by the fact that O 2 adsorption gains electrons from the surface while H 2 O donates electrons to the surface. These results suggest that a more negatively charged site would be more active for the ORR. Our work emphasizes the importance of kinetic information in understanding and designing heterogeneous electrocatalysts.</p></div>
<div xmlns="http://www.tei-c.org/ns/1.0"><head>&#9632; ASSOCIATED CONTENT</head><p>* s&#305; Supporting Information</p><p>The Supporting Information is available free of charge at <ref type="url">https://pubs.acs.org/doi/10.1021/jacs.3c09193</ref>.</p><p>General settings of DFT calculations; details of electronic charge calculation; structure evolution for water adsorption dynamics; details of energy barrier calculations; more reaction kinetics data; and adsorption energies and electronic charge transfer of ORR intermediates (PDF)</p></div><note xmlns="http://www.tei-c.org/ns/1.0" place="foot" xml:id="foot_0"><p>https://doi.org/10.1021/jacs.3c09193 J. Am. Chem. Soc. 2023, 145, 25352-25356</p></note>
			<note xmlns="http://www.tei-c.org/ns/1.0" place="foot" xml:id="foot_1"><p>Journal of the American Chemical Society</p></note>
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