Unraveling the CO Oxidation Mechanism over Highly Dispersed Pt Single Atom on Anatase TiO2 (101)

锐钛矿 吸附 催化作用 离解(化学) 密度泛函理论 催化循环 金属 化学 贵金属 反应机理 无机化学 氧化还原 物理化学 光化学 光催化 计算化学 有机化学
作者
Celine Tesvara,Md Raian Yousuf,Malik Albrahim,Diego Troya,Abhijit Shrotri,Eli Stavitski,Ayman M. Karim,Philippe Sautet
出处
期刊:ACS Catalysis [American Chemical Society]
卷期号:14 (10): 7562-7575 被引量:5
标识
DOI:10.1021/acscatal.4c01018
摘要

Catalysts with noble metals deposited as single atoms on metal oxide supports have recently been studied extensively due to their maximized metal utilization and potential for performing difficult chemical conversions owing to their unique electronic properties. Understanding of the reaction mechanisms on supported single-metal atoms is still limited but is highly important for designing more efficient catalysts. In this study, we report the complexity of the CO oxidation reaction mechanism on Pt single atoms supported on anatase TiO2 (PtSA/a-TiO2) by coupling density functional theory (DFT) calculations and microkinetic analysis with kinetic measurements, in situ/operando infrared, and X-ray absorption spectroscopies. Starting from the adsorbed PtSA occupying an O vacancy induced by reductive pretreatment, we show that CO oxidation follows a complex mechanism consisting of initiation steps to reorganize the active site and multibranch reactive cycles, with the PtSA/a-TiO2 catalyst not returning to its initial configuration. The initiation step consists of CO and O2 adsorption healing the O vacancy, followed by CO oxidation using gas-phase CO to form Pt(CO). The reactive cycle alternates O2 adsorption and dissociation to oxidize the catalyst to Pt(O)(O)(CO) and branching pathways of competing Langmuir–Hinshelwood (LH)- or Eley–Rideal (ER)-type CO oxidation steps to reduce it again to Pt(CO). In situ/operando infrared experiments, including cryogenic CO adsorption and isotopic CO exchange, confirm the combined involvement of strongly adsorbed CO and gas-phase CO in an Eley–Rideal step along the reaction cycle. Microkinetic modeling shows that Pt single atoms are present in a mixture of Pt(CO), Pt(CO)(O2), Pt(O)(CO)(O2), and Pt(CO)(CO3) structures as the main intermediates during steady-state CO oxidation, all having the C–O vibrational stretch close to the experimentally observed value of 2115 cm–1. Microkinetic modeling also shows that the fractional orders of CO and O2 measured experimentally originate from multiple steps with a high degree of rate control and not from a simple competitive adsorption. The results demonstrate the complex reaction pathways that even CO oxidation on a simple single-atom system can follow, providing mechanistic insights for designing efficient Pt-based single-atom catalysts. We further show that microkinetic modeling results are sensitive to changes in energies of intermediate and transition states within errors of density functional theory, which can ultimately lead to incorrect conclusions regarding the reaction pathways and most abundant reaction intermediates if not accounted for by experiments.
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