Ni/Co in and on CeO2: a comparative study on the dry reforming reaction

被引:4
|
作者
Yadav, Pradeep Kumar [1 ]
Patrikar, Kalyani [1 ]
Mondal, Anirban [1 ]
Sharma, Sudhanshu [1 ]
机构
[1] Indian Inst Technol Gandhinagar, Dept Chem, Gandhinagar 382355, India
关键词
METAL-SUPPORT INTERACTION; CARBON-DIOXIDE; SYNTHESIS GAS; CATALYTIC PERFORMANCE; HYDROGEN-PRODUCTION; CO OXIDATION; DEFECT SITES; METHANE; NI; TRANSIENT;
D O I
10.1039/d3se00649b
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
Mono metal (Ni, Co)-substituted (in) and supported (on) CeO2 catalysts were prepared by using solution combustion synthesis and formaldehyde reduction methods. The catalysts were completely characterized by both bulk and surface techniques. Both supported and substituted catalysts show distinct differences in the dry reforming of methane (DRM) activity. Co-substituted CeO2 showed the highest stability under the DRM reaction conditions at 800 & DEG;C. Detailed kinetic investigations were also carried out to estimate the apparent activation energy. Carbon deposition on the spent catalysts was investigated by thermal gravimetric analysis (TGA) and TEM which shows that the deactivation is due to the presence of amorphous and graphitic carbon. Transient studies on a mass spectrometer indicate that the prominence of the reaction CO2 + C & RARR; 2CO is responsible for the catalyst's stability. Surface lattice oxygen reactivity is a vital factor in catalytic stability and its action decides the reaction steps. DFT further verifies that the energy of vacancy formation is significantly lower in Co-substituted CeO2 as compared to Ni-substituted CeO2. This confirms that the Co-substituted catalyst favors oxidation due to higher availability of surface oxygen, while in contrast Ni hinders oxidation by decreasing the availability of surface oxygen for the reaction.
引用
收藏
页码:3853 / 3870
页数:18
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