化学链燃烧
甲烷
氧气
甲烷氧化偶联
化学
联轴节(管道)
化学工程
环境科学
环境化学
材料科学
有机化学
工程类
冶金
作者
D. H. Guan,Shengpeng Xia,Yunfei Gao,Yuxuan Xu,Jiaxiang Li,Chenkai Sun,Xing Zhu,Zengli Zhao,Anqing Zheng,Kun Zhao
标识
DOI:10.1021/acssuschemeng.5c01466
摘要
The production of olefins via the oxidative coupling of methane (OCM) has been extensively studied. However, the inherent “trade-off” in the OCM limits ethylene yield and selectivity. CO2-assisted OCM provides an opportunity to overcome this limitation by using CO2 as a weak oxidant. Here, we reported a CO2-assisted chemical looping oxidative coupling of methane (CO2–CLOCM) approach using MnO–Na2WO4/SiO2 as the oxygen carrier. The results demonstrated that MnO–Na2WO4/SiO2 manifested superior catalytic performance, achieving 14.29% methane conversion, 0.6224 mmol·g–1·h–1 C2+ production rate, and 3.01% CO2 conversion. Compared to the CLOCM reaction without CO2 assistance, the methane conversion recorded a relative increase of 26.57%, the C2+ production rate showed a relative increase of 21.37%, and the olefin purity in the product increased from 53% to 81%. Introduction of CO2 regulated oxygen release kinetics during the CLOCM process, replenishing lattice oxygen on the oxygen carrier and thereby enhancing methane conversion and C2+ production rates. At elevated temperatures, competitive interactions between CH4 and CO2 for active sites became evident, manifesting ″trade-off ″ in their respective conversion. Isotope-labeling experiments conducted to investigate the CH4–CO2 reaction pathways revealed intricate interactions on the oxygen carrier’s surface, where CO2 engages in thorough oxygen exchange with the carrier.
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