部分氧化
合成气
甲烷
催化作用
化学工程
金属
材料科学
原材料
化学
产量(工程)
碳纤维
反应机理
化学计量学
甲烷氧化偶联
无机化学
甲烷转化炉
多相催化
动力学
过渡金属
氧化还原
化学动力学
作者
Wen Liu,Siqi Tang,Wenqi Sang,Chen Fan,Xizhe Zhang,Weixin Xu,Shuangmei Han,Jianguo Jiang,Sicong Tian,Lujia Han
标识
DOI:10.1002/anie.202518088
摘要
Abstract Partial oxidation reforming of methane provides stoichiometrically optimal syngas as an alternative feedstock for the chemical industry currently relying on coal and petroleum resources. However, effective catalysis at moderate temperatures has been challenging. We report an active‐site shifting mechanism that inherently couples metallic and oxidative catalysis for efficient methane reforming, achieving a syngas yield of 9.7 millimoles per gram of the developed Ni‐FeO x catalyst at 89.9% methane conversion below 700 °C. The discovered mechanism features the ongoing transfer of CH 3 * species from metallic Ni to FeO x , enabling both superior reaction kinetics by prompt liberation of occupied Ni sites and intrinsic avoidance of the intractable carbon deposition. Charge orientational distribution due to the electronic interaction between metallic Ni and FeO x induces the fundamental force driving active‐site shifting. This study substantiates an efficient methane partial oxidation pathway that is distinct from those based on the prevailing tandem‐reaction hypothesis in the coupled catalysis, offering new insights into the catalyst design by active‐site modulation.
科研通智能强力驱动
Strongly Powered by AbleSci AI