Recent advances in promoting dry reforming of methane using nickel-based catalysts

被引:7
|
作者
Zhu, Haibin [1 ]
Chen, Huichao [1 ]
Zhang, Menghan [1 ]
Liang, Cai [1 ]
Duan, Lunbo [1 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Nanjing 210096, Peoples R China
基金
中国国家自然科学基金; 美国国家科学基金会;
关键词
ONE-POT SYNTHESIS; NI-BASED CATALYSTS; CARBON-DIOXIDE; HYDROGEN-PRODUCTION; SYNGAS PRODUCTION; BIMETALLIC CATALYSTS; NI/SIO2; CATALYST; ALLOY CATALYSTS; SUPPORTED NI; PERFORMANCE;
D O I
10.1039/d3cy01612a
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Dry reforming of methane (DRM) is an efficient way for CO2 utilization to convert CH4 and CO2 to syngas (H2 and CO), which is an ingredient to produce hydrogen and methanol and hydrocarbons via Fischer-Tropsch process. Considerable attention is drawn to Ni-based catalyst due to its remarkable reactivity for CH4 and CO2 conversion. However, the weakness of sintering and coking restrains its industrial applications. The successful design of cost-effective, efficient and stable Ni-based catalysts would be a grand breakthrough for the technology. Herein, the thermodynamic analysis and the mechanisms of sintering and coking are presented. Then, the strategies for improving the performance of catalysts are elaborated as follows, with 1) supports improving the particle dispersion of nickels and changing the reaction process for the hindrance of coking; 2) promoters for regulating the nickel's chemical properties to enable catalytic DRM performance; 3) catalysts obtained by varied preparation methods possess different sizes and interactions. Finally, the challenges and future perspectives are highlighted. The achievements of dry reforming of methane over Ni-based catalysts are presented with focus on the modification factors to enhance sintering and coking resistance, elaborated in the context of support, promoter, and preparation.
引用
收藏
页码:1712 / 1729
页数:18
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