Overall
- Language
- English
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
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Received September 30, 2025
Revised November 3, 2025
Accepted November 19, 2025
Available online March 25, 2026
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This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits
unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Most Cited
Structural and Catalytic Eff ect of Fe and Co Incorporation into CeVO 4 for NH 3 -SCR Process
https://doi.org/10.1007/s11814-025-00611-0
Abstract
Selective catalytic reduction is widely applied to various industries for NO x removal. In this study, CeVO 4 -based catalysts
were modifi ed with iron and cobalt to enhance catalytic activity. Each transition metal was partially substituted into either
the Ce or V site at 0.2 molar ratio. The synthesized catalysts exhibited both partial incorporation of the transition metal
into the CeVO4 lattice and the formation of secondary metal oxide phases. In particular, the V site substitution led to
lattice expansion, CeO2 formation, and smaller particle sizes, while the Ce site substitution caused lattice contraction and
larger particle sizes. All of the catalysts were coated on the alumina pellets to protect the reactor from increasing pressure
during the catalytic reduction reaction and boost the catalytic activities, that were evaluated under both oxygen absence
and 1 mol% oxygen fl ow conditions. Among them, CeVO4 -CeO2 -Co3V2 O 8 /Al2O3 catalyst (Ce:V:Co = 1:0.8:0.2 molar
ratio) exhibited the highest NO conversion. This result was attributed to synergistic eff ects, including the promotional
eff ect of CeO2 , and enhanced oxygen migration via the asymmetric Co3+ -O-V5+ phase. Therefore, the transition metal
incorporation, particularly Co substitution at V sites, eff ectively enhances the catalytic activity of CeVO 4 -based catalysts
in the NH 3 -SCR process.

