2024
DOI: 10.1016/j.cattod.2024.114720
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Synergistic effect of Ni and CeOx in NiCeOx/SSZ-13 catalyst for boosting activity and stability during dry reforming of methane

Dawei Han,
Yitao Yang,
Tongtong Wu
et al.
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“…Amvrosios et al [100] prepared Ni/LnOx-type catalysts (Ln = La, Ce, Sm, or Pr) via a citrate sol-gel method and evaluated the dry reforming of methane. It was found that despite the high oxygen storage capacity and redox properties of CeO 2 [101,102], the Ni/CeO 2 catalyst showed lower CH 4 and CO 2 conversion values (just 13% and 35%, respectively) at the conditions of 750 • C, Ar/CH 4 /CO 2 = 2.5:1.5:1, and WGHSV = 200,000 mL g −1 h −1 , a much lower H 2 /CO ratio between 0.3 and 0.6, and high amounts of coke deposits, making it the worst-performing catalyst. The specific surface area of the Ni/CeO 2 catalyst was 3 m 2 g −1 , while the specific surface area of the Ni/La 2 O 3 catalyst was 15 m 2 g −1 .…”
Section: Stability Performance Of La Addition In Ni-based Catalysts F...mentioning
confidence: 99%
“…Amvrosios et al [100] prepared Ni/LnOx-type catalysts (Ln = La, Ce, Sm, or Pr) via a citrate sol-gel method and evaluated the dry reforming of methane. It was found that despite the high oxygen storage capacity and redox properties of CeO 2 [101,102], the Ni/CeO 2 catalyst showed lower CH 4 and CO 2 conversion values (just 13% and 35%, respectively) at the conditions of 750 • C, Ar/CH 4 /CO 2 = 2.5:1.5:1, and WGHSV = 200,000 mL g −1 h −1 , a much lower H 2 /CO ratio between 0.3 and 0.6, and high amounts of coke deposits, making it the worst-performing catalyst. The specific surface area of the Ni/CeO 2 catalyst was 3 m 2 g −1 , while the specific surface area of the Ni/La 2 O 3 catalyst was 15 m 2 g −1 .…”
Section: Stability Performance Of La Addition In Ni-based Catalysts F...mentioning
confidence: 99%