Huang Xin, Eggart Daniel, Qin Gangqiang, Sarma Bidyut Bikash, Gaur Abhijeet, Yang Jiuzhong, Pan Yang, Li Mingrun, Hao Jianqi, Yu Hongfei, Zimina Anna, Guo Xiaoguang, Xiao Jianping, Grunwaldt Jan-Dierk, Pan Xiulian, Bao Xinhe
State Key Laboratory of Catalysis, 2011-Collaborative Innovation Center of Chemistry for Energy Materials, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian, 116023, China.
Institute for Chemical Technology and Polymer Chemistry, Karlsruhe Institute of Technology, Karlsruhe, 76131, Germany.
Nat Commun. 2023 Sep 15;14(1):5716. doi: 10.1038/s41467-023-41192-y.
Molybdenum supported on zeolites has been extensively studied as a catalyst for methane dehydroaromatization. Despite significant progress, the actual intermediates and particularly the first C-C bond formation have not yet been elucidated. Herein we report evolution of methyl radicals during non-oxidative methane activation over molybdenum single sites, which leads selectively to value-added chemicals. Operando X-ray absorption spectroscopy and online synchrotron vacuum ultraviolet photoionization mass spectroscopy in combination with electron microscopy and density functional theory calculations reveal the essential role of molybdenum single sites in the generation of methyl radicals and that the formation rate of methyl radicals is linearly correlated with the number of molybdenum single sites. Methyl radicals transform to ethane in the gas phase, which readily dehydrogenates to ethylene in the absence of zeolites. This is essentially similar to the reaction pathway over the previously reported SiO lattice-confined single site iron catalyst. However, the availability of a zeolite, either in a physical mixture or as a support, directs the subsequent reaction pathway towards aromatization within the zeolite confined pores, resulting in benzene as the dominant hydrocarbon product. The findings reveal that methyl radical chemistry could be a general feature for metal single site catalysis regardless of the support (either zeolites MCM-22 and ZSM-5 or SiO) whereas the reaction over aggregated molybdenum carbide nanoparticles likely facilitates carbon deposition through surface C-C coupling. These findings allow furthering the fundamental insights into non-oxidative methane conversion to value-added chemicals.
负载在沸石上的钼作为甲烷脱氢芳构化催化剂已得到广泛研究。尽管取得了显著进展,但实际的中间体,特别是第一个碳 - 碳键的形成尚未阐明。在此,我们报告了在钼单中心上非氧化甲烷活化过程中甲基自由基的演变,这一过程选择性地生成了高附加值化学品。原位X射线吸收光谱、在线同步辐射真空紫外光电离质谱结合电子显微镜和密度泛函理论计算揭示了钼单中心在甲基自由基生成中的关键作用,并且甲基自由基的形成速率与钼单中心的数量呈线性相关。甲基自由基在气相中转化为乙烷,在没有沸石的情况下,乙烷很容易脱氢生成乙烯。这与先前报道的SiO晶格限制单中心铁催化剂上的反应途径基本相似。然而,无论是以物理混合物形式还是作为载体存在的沸石,都会引导后续反应途径朝着沸石限制孔内的芳构化方向进行,从而使苯成为主要的烃类产物。研究结果表明,甲基自由基化学可能是金属单中心催化的一个普遍特征,而与载体(无论是沸石MCM - 22和ZSM - 5还是SiO)无关,而在聚集的碳化钼纳米颗粒上的反应可能通过表面碳 - 碳偶联促进碳沉积。这些发现有助于进一步深入了解非氧化甲烷转化为高附加值化学品的过程。