甲烷
化学计量学
非阻塞I/O
二氧化碳重整
催化作用
金属
无机化学
材料科学
化学工程
化学
冶金
合成气
有机化学
工程类
作者
Yongtak Kwon,J. Ehren Eichler,C. Buddie Mullins
标识
DOI:10.1016/j.jcou.2022.102112
摘要
We have studied the catalytic behavior of different Ni/Al 2 O 3 catalysts for the dry reforming of methane which originate from different Ni metal sources: NiO and also non-stoichiometric and stoichiometric NiAl 2 O 4 . After complete reduction of the stoichiometric NiAl 2 O 4 precursor at high temperatures, the resulting Ni/Al 2 O 3 catalyst had more dispersed Ni particles of smaller size and with stronger interactions with alumina. Accordingly, this catalyst was more active and stable, developing only a moderate amount of carbon deposits which were less graphitized. On the other hand, the catalyst formed from NiO showed low initial activity and notable deactivation resulting from the encapsulation and separation of Ni metal particles from the support by more graphitic carbons, which was facilitated by the weaker metal-support interactions. In contrast to what is frequently reported, here we provide evidence which suggests that the NiAl 2 O 4 species should be considered the most beneficial precursor for Ni metal in a Ni/Al 2 O 3 catalyst for the dry reforming of methane even though a high reduction temperature (>950 °C) is needed to activate it. • The origin of Ni metal influences the property of the reduced Ni/Al 2 O 3 catalyst. • The NiAl 2 O 4 phase showed the most active, selective, and highly stable performance. • The NiO phase showed the lowest activity and significant deactivation by coking. • NiAl 2 O 4 is the most advantageous precursor for Ni in a Ni/Al 2 O 3 catalyst for DRM.
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