Qi Wenjie, Huang Zehao, Chen Zheming, Fu Lijuan, Zhang Zhigang
Key Laboratory of Advanced Manufacturing Technology for Automobile Parts, Ministry of Education, Chongqing University of Technology Chongqing 400050 China
Department of Chemistry, Fujian Province University Key Laboratory of Green Energy and Environment Catalysis, Ningde Normal University Ningde 352100 People's Republic of China.
RSC Adv. 2019 Apr 11;9(20):11385-11395. doi: 10.1039/c9ra00735k. eCollection 2019 Apr 9.
Density functional theory (DFT) and measurements of rate are used to provide evidence for the rate determining step (RDS) and requirements of the active site for CH combustion on Pd-Pt bimetallic catalysts in five different distinct kinetic regimes. These five regimes exhibit different rate equations for methane combustion due to the reaction rate constants and diverse dominant adsorbed species for these different kinetically relevant steps. Oxygen chemical potential at the Pd-Pt surface was replaced by oxygen pressure, reflecting the kinetic coupling between C-H and O[double bond, length as m-dash]O bond cleavage steps. C-H bond cleavage occurs on different active sites in five of these kinetic regimes, evolving from vacancy-vacancy (-) to oxygen-vacancy (O*-), oxygen-oxygen (O-O*) site pairs, monolayer Pd-O, and ultimately to oxide bulk with Pd-O site pairs as the oxygen chemical potential increases. It is easier to form a metallic surface at low oxygen pressure, implying minimal O* coverage. The sole kinetically relevant step on uncovered Pd-Pt surfaces for methane combustion is O[double bond, length as m-dash]O bond cleavage. The supply of oxygen is obviously more important than the supply of methane in regime (I). As vacancies become less available on metallic surfaces, C-H bond cleavage occurs O*-* paired sites, the energy barrier of which is much higher than that on uncovered Pd-Pt surfaces. In this regime (II), O[double bond, length as m-dash]O bond cleavage is still an irreversible process because O* will be consumed by the rapidly formed products of methane dissociation. For the oxygen saturated surfaces in regime (III), C-H bond cleavage occurs on two adjacent adsorbed oxygens that form OH and weak CH-O bond interactions, resulting in a low activity for methane combustion. On the oxidation surfaces (IV and V), exposed metal atoms and their adjacent exposed lattice oxygen were the active sites, leading to a large decrease in C-H bond cleavage energy barrier, deduced from both experiment and theory. The increase of the metallic oxide thickness (increase of oxygen potential) increases the methane combustion turnover rates on Pd-Pt catalysts.
密度泛函理论(DFT)和速率测量用于为钯 - 铂双金属催化剂上甲烷燃烧的速率决定步骤(RDS)以及活性位点的要求提供证据,该过程处于五种不同的动力学区域。由于这些不同动力学相关步骤的反应速率常数和多种占主导的吸附物种,这五种区域表现出不同的甲烷燃烧速率方程。钯 - 铂表面的氧化学势被氧分压所取代,这反映了C - H键和O = O键断裂步骤之间的动力学耦合。在这些动力学区域中的五个区域里,C - H键断裂发生在不同的活性位点上,随着氧化学势的增加,从空位 - 空位(* - )演变为氧 - 空位(O - )、氧 - 氧(O - O*)位点对、单层Pd - O,最终演变为具有Pd - O位点对的氧化物块体。在低氧分压下更容易形成金属表面,这意味着O覆盖率最小。对于未覆盖的钯 - 铂表面上甲烷燃烧唯一的动力学相关步骤是O = O键断裂。在区域(I)中,氧气的供应显然比甲烷的供应更重要。随着金属表面上空位变得更少,C - H键断裂发生在O - 配对位点上,其能垒远高于未覆盖的钯 - 铂表面上的能垒。在这个区域(II)中,O = O键断裂仍然是一个不可逆过程,因为O会被甲烷解离快速形成的产物消耗。对于区域(III)中氧饱和的表面,C - H键断裂发生在两个相邻的吸附氧上,形成OH和弱的CH - O键相互作用,导致甲烷燃烧活性较低。在氧化表面(IV和V)上,暴露的金属原子及其相邻的暴露晶格氧是活性位点,从实验和理论推导都导致C - H键断裂能垒大幅降低。金属氧化物厚度的增加(氧势的增加)提高了钯 - 铂催化剂上甲烷燃烧的周转速率。