ORIGINAL RESEARCH
Study on Low-Temperature Methanation
of Coal Pyrolysis Gas over Ni-Based
Catalysts with Core-Shell Structure
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1
College of Energy and Chemical Engineering, Xinjiang Institute of Technology, Aksu 843100, China
2
Xinjiang Key Laboratory of New Energy and Energy Storage Technology, Xinjiang Institute of Technology,
Aksu 843100, China
Submission date: 2025-11-13
Final revision date: 2026-02-02
Acceptance date: 2026-03-31
Online publication date: 2026-07-30
Corresponding author
Jihao Chen
College of Energy and Chemical Engineering, Xinjiang Institute of Technology, Aksu 843100, China
Ye Li
College of Energy and Chemical Engineering, Xinjiang Institute of Technology, Aksu 843100, China
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ABSTRACT
In this study, a series of SiO2@ZrO2-supported catalysts was employed for the methanation
of CO/CO2 in a fixed-bed reactor to address the issues of insufficient low-temperature activity and sulfur
poisoning of catalysts during CO/CO2 methanation. Mesoporous SiO2@ZrO2 core–shell supports were
prepared via the sol-gel method and liquid-phase coating process, and Ni-CeO2-ZnO catalysts supported
on SiO2@ZrO2 were synthesized by incipient wetness impregnation with Ni as the active component
and CeO2-ZnO as promoters. Catalysts with optimal methanation performance and sulfur resistance
were screened by regulating the ZrO2 shell loading (7%, 15%, 23%), Ni loading (5%, 10%, 15%, 20%),
and Ce/Zn promoter molar ratio (3:1, 1:1, 1:3). The structural properties and catalytic mechanism were
analyzed using multiple characterization techniques, including XRD, SEM, TEM, XPS, and H2-TPR.
The results showed that: (1) the Ni-CeO2-ZnO/SiO2@ZrO2 catalyst achieved CO and CO2 conversions of
92.37% and 87.63%, respectively, with CH4 selectivity exceeding 99%; after exposure to 50 ppm H2S,
the catalyst retained 85% of its initial activity in a 500 h stability test. (2) Characterization revealed
that the mesoporous SiO2@ZrO2 support suppressed Ni sintering and accelerated mass transfer;
ZnO preferentially adsorbed H2S to form ZnS, protecting the Ni active sites, thereby enabling efficient
CO/CO2 methanation and sulfur resistance of the catalyst.
CONFLICT OF INTEREST
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
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