Journal
KOREAN JOURNAL OF CHEMICAL ENGINEERING
Volume 34, Issue 12, Pages 3085-3091Publisher
KOREAN INSTITUTE CHEMICAL ENGINEERS
DOI: 10.1007/s11814-017-0257-0
Keywords
CO Methanation; CO2 Methanation; Ni/Al2O3; Alumina; Crystalline Phase
Funding
- Human Resources Program in Energy Technology of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) - Ministry of Trade, Industry and Energy of the Republic of Korea [20154010200820]
- Basic Science Research Program through the National Research Foundation of Korea (NRF) - Ministry of Science and ICT [2017R1A2B3011316]
- National Research Foundation of Korea [2017R1A2B3011316] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)
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The effect of alumina crystalline phases on CO and CO2 methanation was investigated using alumina-supported Ni catalysts. Various crystalline phases, such as alpha-Al2O3, theta-Al2O3, delta-Al2O3, eta-Al2O3, gamma-Al2O3, and kappa-Al2O3, were utilized to prepare alumina-supported Ni catalysts via wet impregnation. N-2 physisorption, H-2 chemisorption, temperature-programmed reduction with H-2, CO2 chemisorption, temperature-programmed desorption of CO2, and X-ray diffraction were employed to characterize the catalysts. The Ni/theta-Al2O3 catalyst showed the highest activity during both CO and CO2 methanation at low temperatures. CO methanation catalytic activity appeared to be related to the number of Ni surface-active sites, as determined by H-2-chemisorption. During CO2 methanation, Ni dispersion and the CO2 adsorption site were found to influence catalytic activity. Selective CO methanation in the presence of excess CO2 was performed over Ni/gamma-Al2O3 and Ni/delta-Al2O3; these substrates proved more active for CO methanation than for CO2 methanation.
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