二氧化碳重整
甲烷
催化作用
材料科学
化学工程
碳纤维
吸附
原材料
钙钛矿(结构)
合成气
密度泛函理论
甲烷转化炉
二氧化碳
温室气体
氧气
无机化学
蒸汽重整
纳米技术
多相催化
作者
Chencun Hao,Zhiyu Qu,Louise R. Smith,Nicholas F. Dummer,Haifeng Qi,Thomas J. A. Slater,Zhiping Zhu,Riguang Zhang,Zhao Sun,Zhiqiang Sun,Graham J. Hutchings
标识
DOI:10.1038/s41467-025-65619-w
摘要
Abstract Dry reforming of methane is an effective approach to convert two major greenhouse gases, methane and carbon dioxide, into high-value syngas, used as a feedstock for bulk and fine chemical synthesis. However, catalyst deactivation and carbon deposition under harsh conditions hinder its industrialization process. Herein, we present a Ce-modified and Ni-exsolved perovskite catalyst, 0.2Ce-La 0.97 Ni 0.4 Cr 0.6 O 3 , for achieving highly efficient and robust CH 4 -CO 2 reforming with CH 4 and CO 2 conversions of 87.4% and 92.9% at 800 °C, respectively. Moreover, this unique catalyst exhibits remarkable stability, maintaining its superior activity over 800 h. Characterization and density functional theory reveal that two Ce species are present: surface oxygen vacancy-moderate CeO 2- x (Ce surf ) and bulk lattice Ce (Ce bulk ). These play a specific role in methane dry reforming, where the Ce surf promotes CO 2 adsorption and hinders carbon deposition, while Ce bulk induces lattice strain and Ni exsolution, key factors contributing to the high activity and stability.
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