The methanation of carbon dioxide via the Sabatier process is attracting growing attention for power-to-gas (P2G) application. In the current study, a series of 25 wt% Ni-based catalysts were synthesized using solution combustion synthesis (SCS) to investigate the influence of the support on the methanation performance. The results showed that Ni/CeO2-ZrO2 catalyst exhibited superior activity, achieving 72.5 % and 95.5 % CO2 conversion at 250 degrees C and 300 degrees C, respectively, while maintaining excellent stability over 100 h of time-on-stream. CO2-TPD analysis revealed that weak-to-moderate basic sites played a key role in enhancing catalytic activity. This is consistent with XPS results, which indicated a high concentration of surface hydroxyl groups and oxygen vacancies, responsible for the enhanced basicity of the CeO2-ZrO2 support. Additionally, the CO-chemisorption measurements confirmed improved Ni dispersion, further contributing to efficient H2 activation. In situ DRIFTMS studies identified a reaction pathway involving CO2 adsorption as carbonate and bicarbonate species, followed by stepwise hydrogenation to methane via formate intermediates. The correlation between turnover frequency (TOF) and the number of weak-to-moderate basic sites supports a dual-site reaction mechanism, where basic sites facilitate CO2 activation and Ni sites promote H2 dissociation, both contributing to the remarkable low-temperature carbon dioxide methanation activity.

Enhanced low-temperature activity of CO2 methanation: Effect of metal oxide support on the performance of Ni-based catalysts

Italiano C.
;
Pino L.;Maccarrone D.;Vita A.
Ultimo
2025

Abstract

The methanation of carbon dioxide via the Sabatier process is attracting growing attention for power-to-gas (P2G) application. In the current study, a series of 25 wt% Ni-based catalysts were synthesized using solution combustion synthesis (SCS) to investigate the influence of the support on the methanation performance. The results showed that Ni/CeO2-ZrO2 catalyst exhibited superior activity, achieving 72.5 % and 95.5 % CO2 conversion at 250 degrees C and 300 degrees C, respectively, while maintaining excellent stability over 100 h of time-on-stream. CO2-TPD analysis revealed that weak-to-moderate basic sites played a key role in enhancing catalytic activity. This is consistent with XPS results, which indicated a high concentration of surface hydroxyl groups and oxygen vacancies, responsible for the enhanced basicity of the CeO2-ZrO2 support. Additionally, the CO-chemisorption measurements confirmed improved Ni dispersion, further contributing to efficient H2 activation. In situ DRIFTMS studies identified a reaction pathway involving CO2 adsorption as carbonate and bicarbonate species, followed by stepwise hydrogenation to methane via formate intermediates. The correlation between turnover frequency (TOF) and the number of weak-to-moderate basic sites supports a dual-site reaction mechanism, where basic sites facilitate CO2 activation and Ni sites promote H2 dissociation, both contributing to the remarkable low-temperature carbon dioxide methanation activity.
2025
Istituto di Tecnologie Avanzate per l'Energia - ITAE
CO2 methanation
Ni catalysts
Support effect
Power-to-gas
SNG production
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/558557
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