Mechanism Explorationof the Water–Gas ShiftReaction on Cu<sub>4</sub>/CeO<sub>2</sub>(110) under Realistic ReactionTemperatures

The dynamic evolution of catalysts has a significant impact on the catalytic activity. Herein, we report the dynamic structure of Cu<sub>4</sub>/CeO<sub>2</sub>(110) at real water–gas shift reaction (WGSR) reaction temperatures and its influence on the WGSR activity in terms of both ab initio molecular dynamics (AIMD) and density functional theory (DFT) calculation. At the reaction temperature (523 K) or catalyst preparation temperature (773 K), reverse spillover of lattice oxygen atoms was observed at the Ce–Cu interface, leaving the corresponding oxygen vacancy (O<sub>V</sub>) by AIMD, wherein the interfacial spillover oxygen atoms (O<sub>sp</sub>) were proved to be the result of the high active surface of CeO<sub>2</sub>(110) and have the function of providing structure support, promoting metal–support interaction (MSI), and inducing steric effect to facilitate H<sub>2</sub>O adsorption and COOH formation. Moreover, the charge analysis revealed the MSI trend of Cu<sub>4</sub>/CeO<sub>2</sub>(110), following the order of 773 K > 523 K > 0 K (i.e., standard DFT-optimized result). Microkinetic modeling showed the catalytic superiority of the 523 K model, followed by 0 K, indicating that MSI should be adjusted to a moderate level. Instead, when the cluster is passivated or shows a low adsorption strength, the active center is transferred to the Cu–O<sub>V</sub>–Ce interface site. Interestingly, we found that the 773 K model would promote its activity drastically through O<sub>sp</sub> hydroxylation, which would improve the activity of the cluster and avoid water decomposition at the O<sub>sp</sub> site, further elevating the production. This work highlights the role of moderate MSI and alternative active centers of the interface in WGSR on supported catalysts. It provides new insights into catalyst design and mechanism exploration for WGSR.

Publication Details

Journal
Figshare
Published
2025-02-27
DOI
https://doi.org/10.1021/acs.jpcc.4c08279.s001
Primary Topic
Educational Robotics and Engineering
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article
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article

Mechanism Explorationof the Water–Gas ShiftReaction on Cu4/CeO2(110) under Realistic ReactionTemperatures

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Educational Robotics and Engineering
article

Mechanism Explorationof the Water–Gas ShiftReaction on Cu4/CeO2(110) under Realistic ReactionTemperatures

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Abstract

The dynamic evolution of catalysts has a significant impact on the catalytic activity. Herein, we report the dynamic structure of Cu<sub>4</sub>/CeO<sub>2</sub>(110) at real water–gas shift reaction (WGSR) reaction temperatures and its influence on the WGSR activity in terms of both ab initio molecular dynamics (AIMD) and density functional theory (DFT) calculation. At the reaction temperature (523 K) or catalyst preparation temperature (773 K), reverse spillover of lattice oxygen atoms was observed at the Ce–Cu interface, leaving the corresponding oxygen vacancy (O<sub>V</sub>) by AIMD, wherein the interfacial spillover oxygen atoms (O<sub>sp</sub>) were proved to be the result of the high active surface of CeO<sub>2</sub>(110) and have the function of providing structure support, promoting metal–support interaction (MSI), and inducing steric effect to facilitate H<sub>2</sub>O adsorption and COOH formation. Moreover, the charge analysis revealed the MSI trend of Cu<sub>4</sub>/CeO<sub>2</sub>(110), following the order of 773 K > 523 K > 0 K (i.e., standard DFT-optimized result). Microkinetic modeling showed the catalytic superiority of the 523 K model, followed by 0 K, indicating that MSI should be adjusted to a moderate level. Instead, when the cluster is passivated or shows a low adsorption strength, the active center is transferred to the Cu–O<sub>V</sub>–Ce interface site. Interestingly, we found that the 773 K model would promote its activity drastically through O<sub>sp</sub> hydroxylation, which would improve the activity of the cluster and avoid water decomposition at the O<sub>sp</sub> site, further elevating the production. This work highlights the role of moderate MSI and alternative active centers of the interface in WGSR on supported catalysts. It provides new insights into catalyst design and mechanism exploration for WGSR.

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