二氧化碳重整
催化作用
铈
甲烷
镍
非阻塞I/O
材料科学
氧气
烧结
化学工程
氧化铈
无机化学
合成气
化学
冶金
有机化学
工程类
作者
Xi Ding,Yunfeng Yang,Zhaoyang Li,Pan Huang,Xiaohui Liu,Yong Guo,Yanqin Wang
出处
期刊:ACS Catalysis
日期:2023-11-17
卷期号:13 (23): 15535-15545
被引量:16
标识
DOI:10.1021/acscatal.3c04150
摘要
Nickel, the most commonly used active metal for the dry reforming of methane (DRM), often encounters the challenge of severe deactivation due to sintering and carbon deposition. In this study, we introduce cerium into Ni/MgO, a traditional catalyst for DRM, to improve its activity and stability, resulting in an enhanced Ni/MgCeOx catalyst. With the optimized doping amount of cerium (Ce/Mg = 0.12), the catalyst demonstrates a conversion rate 65% for CH4, 75% for CO2, and a H2/CO ratio of 0.76, while the Ni/MgO catalyst only achieves a conversion rate of 57% for CH4, 65% for CO2, and a H2/CO ratio of 0.68. Furthermore, the introduction of cerium significantly improves the stability of the catalyst. These improved activity and stability can be attributed to the easy reducibility of NiOx species, small Ni particle size, and abundant oxygen vacancies resulting from the doping of cerium. The affinity between CeO2 and NiOx inhibits the formation of the NiO-MgO solid solution, which contributes to the enhanced performance.
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