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Effect of metal loading on the CO2 methanation: A comparison between alumina supported Ni and Ru catalysts.

Authors :
Quindimil, Adrián
De-La-Torre, Unai
Pereda-Ayo, Beñat
Davó-Quiñonero, Arantxa
Bailón-García, Esther
Lozano-Castelló, Dolores
González-Marcos, José A.
Bueno-López, Agustín
González-Velasco, Juan R.
Source :
Catalysis Today. Oct2020, Vol. 356, p419-432. 14p.
Publication Year :
2020

Abstract

• Increasing loading of Ni and Ru increases the surface basicity and forms new CO 2 adsorption sites. • High calcination temperature leads to an increase of RuO 2 particle size and formation of inert Ni species. • Ni/Al 2 O 3 catalysts present high metal-support interaction, so that only a relative amount of metal is active for CO 2 methanation. • Ru/Al 2 O 3 catalysts are more efficient than Ni/Al 2 O 3 in hydrogen dissociation; TOF of the former is about ten times than TOF of Ni catalysts. • Optimal behavior was found for 12% Ni and 4% Ru, which provide metal surfaces of 5.1 and 0.6 m2 g−1, respectively. The hydrogenation of CO 2 into CH 4 from H 2 produced by renewable energy is considered an interesting alternative in order to promote the development of such green energies. In the present work, the effect of Ni and Ru loadings on the catalytic performance of alumina-supported catalysts is studied for CO 2 methanation reaction. All catalysts were prepared by wetness incipient impregnation, characterized by several techniques (N 2 -physisorption, CO 2 -TPD, XRD, H 2 -chemisorption, XPS and H 2 -TPR) and evaluated for CO 2 methanation in a fixed bed reactor at GHSV = 10,000 h−1 and W / F C O 2 0 = 4.7 (g cat.) h mol−1. Characterization results showed that addition of increasing loadings of Ni and Ru lead to the formation of both CO 2 adsorption and H 2 dissociation active sites, which are necessary to carry out CO 2 hydrogenation into methane. Easily reducible ruthenium was dispersed on γ-Al 2 O 3 in form of large agglomerates, whereas Ni was better dispersed presenting a great interaction with the support. 12% Ni and 4% Ru resulted to be the optimal contents providing metal surfaces of 5.1 and 0.6 m2 g−1, T 50 values of 340 and 310 °C and activity being quite stable for 24 h-on-stream. In terms of turnover frequency (TOF), 4%Ru/Al 2 O 3 catalyst was quite more efficient than 12%Ni/Al 2 O 3 , probably due to a greater ability of ruthenium to dissociate hydrogen. The apparent activation energies for alumina supported Ni and Ru were 129 and 84 kJ mol−1, respectively. [ABSTRACT FROM AUTHOR]

Details

Language :
English
ISSN :
09205861
Volume :
356
Database :
Academic Search Index
Journal :
Catalysis Today
Publication Type :
Academic Journal
Accession number :
146534309
Full Text :
https://doi.org/10.1016/j.cattod.2019.06.027