Individual Functionality and Synergistic Effects of Redox Site–Acid Site in Propane Oxidation

IF 13.1 1区 化学 Q1 CHEMISTRY, PHYSICAL
Cai-Hao Wen, Lin-Ya Xu, Yao-Dong Hao, Qian Zhou, Yi-Wei Xian, Mao-Di Wang*, Wei Tan*, Lin Dong, Jian Chen*, Meng-Fei Luo and Qi-Hua Yang, 
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引用次数: 0

Abstract

Catalytic combustion represents one of the most efficient technologies for light-alkane volatile organic compound abatement. However, the reaction mechanisms over heterogeneous catalysts remain controversial, which significantly hinders the rational design of highly efficient and stable catalysts. In this work, it is found that the T50 (the temperature at which propane conversion reached 50%) of Pt/MoO3 (220 °C) is much lower than that of Pt/CeO2 (T50 = 320 °C) in propane combustion (C3H8 + O2 → CO2 + H2O), indicating the possibility of synergistic catalysis occurring between Pt and MoO3 sites. Based on a hybrid catalysis system composed of physically mixed MoO3 and Pt/CeO2 (denoted as Pt/CeO2+MoO3), the critical roles of the acid site from MoO3 for propane activation and the Pt site for oxygen-activation have been originally investigated in propane oxidation, even though Pt and MoO3 sites are spatially separated. The results of the kinetic study, in situ diffuse reflectance infrared Fourier transform spectra of propane combustion, and X-ray photoelectron spectra experiments sufficiently evidenced that propane preferentially absorbs on the MoO3 surface, and the oxygen spillover from Pt sites to the MoO3 surface further facilitates the oxidation of propane. Density functional theory calculations reveal that Pt sites exhibit stronger O2 adsorption, while the synergy between five-coordinated and four-coordinated Mo sites enables MoO3 with an enhanced propane activation capability. That is, MoO3 offers important extra sites for propane activation, effectively avoiding the competitive adsorption between oxygen and propane on the Pt sites. A large distance between MoO3 and Pt sites negatively impacts catalytic activity. Additionally, via construction of defective MoO3 containing more surface acid sites, it is disclosed that stronger surface acidity of MoO3 significantly promotes the catalytic performance of Pt sites and MoO3 sites. This work sheds light on the reaction mechanism of light-alkane oxidation over the metal oxide-supported Pt catalyst.

Abstract Image

丙烷氧化过程中氧化还原位点-酸位点的个体功能和协同效应
催化燃烧是治理轻烷烃挥发性有机化合物最有效的技术之一。然而,多相催化剂上的反应机理仍存在争议,这极大地阻碍了高效稳定催化剂的合理设计。本研究发现,在丙烷燃烧(C3H8 + O2→CO2 + H2O)过程中,Pt/MoO3(220℃)的T50(丙烷转化率达到50%时的温度)远低于Pt/CeO2 (T50 = 320℃),表明Pt和MoO3位点之间可能发生协同催化作用。基于物理混合MoO3和Pt/CeO2 (Pt/CeO2+MoO3)组成的混合催化体系,初步研究了MoO3的酸性位点对丙烷活化的关键作用和Pt的氧活化作用,尽管Pt和MoO3位点在空间上是分开的。丙烷燃烧的动力学研究、原位漫反射红外傅立叶变换光谱和x射线光电子能谱实验结果充分证明了丙烷在MoO3表面优先吸收,并且氧从Pt位溢出到MoO3表面进一步促进了丙烷的氧化。密度泛函理论计算表明,Pt位点表现出更强的O2吸附能力,而五配位和四配位的Mo位点之间的协同作用使MoO3具有更强的丙烷活化能力。也就是说,MoO3为丙烷活化提供了重要的额外位点,有效地避免了氧和丙烷在Pt位点上的竞争性吸附。MoO3和Pt位点之间的较大距离对催化活性有不利影响。此外,通过构建含有更多表面酸性位点的缺陷MoO3,揭示了MoO3表面酸性的增强显著促进了Pt位点和MoO3位点的催化性能。本研究揭示了金属氧化物负载Pt催化剂上轻烷烃氧化反应机理。
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来源期刊
ACS Catalysis
ACS Catalysis CHEMISTRY, PHYSICAL-
CiteScore
20.80
自引率
6.20%
发文量
1253
审稿时长
1.5 months
期刊介绍: ACS Catalysis is an esteemed journal that publishes original research in the fields of heterogeneous catalysis, molecular catalysis, and biocatalysis. It offers broad coverage across diverse areas such as life sciences, organometallics and synthesis, photochemistry and electrochemistry, drug discovery and synthesis, materials science, environmental protection, polymer discovery and synthesis, and energy and fuels. The scope of the journal is to showcase innovative work in various aspects of catalysis. This includes new reactions and novel synthetic approaches utilizing known catalysts, the discovery or modification of new catalysts, elucidation of catalytic mechanisms through cutting-edge investigations, practical enhancements of existing processes, as well as conceptual advances in the field. Contributions to ACS Catalysis can encompass both experimental and theoretical research focused on catalytic molecules, macromolecules, and materials that exhibit catalytic turnover.
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