Performance of CaO-Promoted Ni Catalysts over Nanostructured CeO2 in Dry Reforming of Methane

被引:0
|
作者
Perez-Madrigal, Vicente [1 ]
Santiago-Salazar, Didier [1 ]
Ortega-Aviles, Mayahuel [2 ]
Rios-Valdovinos, Edna [1 ]
Albiter, Elim [3 ]
Valenzuela, Miguel A. [3 ]
Pola-Albores, Francisco [1 ]
机构
[1] Univ Ciencias & Artes Chiapas, Lab Mat & Proc Sustentables, Libramiento Nte Pte 1150,Lajas Maciel, Tuxtla Gutierrez 29039, Chiapas, Mexico
[2] Inst Politecn Nacl, Ctr Nanociencias Micro & Nanotecnolgias, Luis Enr Erro S-N, Mexico City 07738, Mexico
[3] ESIQIE Inst Politecn Nacl, Lab Catalisis & Mat, Mexico City 07738, Mexico
关键词
methane dry reforming; Ni catalysts; surface basicity; promotors; CaO; NI/CEO2-ZRO2; CATALYSTS; COKE FORMATION; SYSTEMS; SITES; MGO;
D O I
10.3390/pr12122815
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Ni (20 wt.%) catalysts supported on CeO2 were synthesized using the incipient wetness impregnation method and promoted with varying amounts of CaO (0, 5, 10, 15, 20 wt.%). The catalysts were evaluated in dry reforming of methane (DRM) at 650 degrees C for 24 h. Fresh catalysts were characterized by XRD, WD-XRF, H2-TPR, N2 physisorption, HDP, SEM, and FT-IR spectroscopy (DRIFT and ATR), while spent catalysts were characterized by XRD, Raman spectroscopy, and SEM. The incorporation of 5-15 wt.% CaO on CeO2 significantly improved its catalytic performance. FT-IR analysis confirmed the presence of CaCO3 bands, indicating carbonate formation. The Ni/CeO2 catalyst with 15 wt.% CaO exhibited the highest catalytic activity. The promoted catalysts demonstrated high stability, attributed to strong interactions between CeO2, CaO, and CaCO3. However, when CaO promotion reached 20 wt.%, catalytic activity decreased. Despite large carbon formations, the catalysts maintained their stability with no significant deactivation due to sintering or coke accumulation.
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页数:15
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