TY - JOUR
T1 - CO2-intensified dry reforming of methane over oxygen-defective Ni-CeO2 catalysts
T2 - Synergistic coupling with reverse water-gas shift reaction
AU - Kim, Beom Jun
AU - Park, Ho Ryong
AU - Ryu, Su Jin
AU - Jeon, Byong Hun
AU - Roh, Hyun Seog
N1 - Publisher Copyright:
© 2025
PY - 2025/2/1
Y1 - 2025/2/1
N2 - This study investigates the performance of Ni-CeO2 catalysts synthesized via a cellulose-assisted combustion method (CACS) for the synergistic coupling of dry reforming of methane (DRM) and the reverse water–gas shift reaction (RWGS), referred to as SCDR. Among the catalysts with varying Ni loadings, the 15 wt% Ni-CeO2 catalyst exhibited an optimal balance of Ni dispersion and oxygen vacancy formation, achieving superior CH4 and CO2 conversions. In DRM reaction, catalytic activity was primarily determined by the number of Ni active sites, with higher Ni dispersion enhancing CH4 conversion. In contrast, under SCDR conditions, catalytic performance was significantly influenced by the oxygen storage capacity (OSC), which facilitated CO2 activation and intermediate formation. The well-dispersed Ni and strong metal-support interaction at the Ni-O-Ce interface further promoted CO2 activation, improving sintering resistance and enabling the formation of key intermediates such as bidentate carbonates and formates. These intermediates were essential for sustaining reaction turnover, with the Ni-O-Ce interface contributing to the rapid regeneration of active sites and maintaining catalytic activity under CO2-rich conditions. Additionally, the high CO2 partial pressure in SCDR suppressed carbon deposition, enhancing stability and reaction rates compared to DRM.
AB - This study investigates the performance of Ni-CeO2 catalysts synthesized via a cellulose-assisted combustion method (CACS) for the synergistic coupling of dry reforming of methane (DRM) and the reverse water–gas shift reaction (RWGS), referred to as SCDR. Among the catalysts with varying Ni loadings, the 15 wt% Ni-CeO2 catalyst exhibited an optimal balance of Ni dispersion and oxygen vacancy formation, achieving superior CH4 and CO2 conversions. In DRM reaction, catalytic activity was primarily determined by the number of Ni active sites, with higher Ni dispersion enhancing CH4 conversion. In contrast, under SCDR conditions, catalytic performance was significantly influenced by the oxygen storage capacity (OSC), which facilitated CO2 activation and intermediate formation. The well-dispersed Ni and strong metal-support interaction at the Ni-O-Ce interface further promoted CO2 activation, improving sintering resistance and enabling the formation of key intermediates such as bidentate carbonates and formates. These intermediates were essential for sustaining reaction turnover, with the Ni-O-Ce interface contributing to the rapid regeneration of active sites and maintaining catalytic activity under CO2-rich conditions. Additionally, the high CO2 partial pressure in SCDR suppressed carbon deposition, enhancing stability and reaction rates compared to DRM.
KW - Cellulose-assisted combustion method
KW - Dry reforming of methane
KW - Oxygen storage capacity
KW - Reverse water–gas shift reaction
KW - Synergistic coupling
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U2 - 10.1016/j.cej.2025.159299
DO - 10.1016/j.cej.2025.159299
M3 - Article
AN - SCOPUS:85214340841
SN - 1385-8947
VL - 505
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 159299
ER -