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Structural Investigation of the Carbon Deposits on Ni/Al2O3 Catalyst Modified by CaO-MgO for the Biogas Dry Reforming Reaction
1 , 1 , 2 , 3 , 3 , 4 , 5 , 6 , * 1
1  University of Western Macedonia, Department of Chemical Engineering
2  University fo Zaragoza, Chemical and Environmental Engineering Department
3  University of Surrey, Faculty of Engineering and Physical Sciences
4  University of Patras, Department of Environmental Engineering
5  Beijing University of Chemical Technology, Biomass Energy and Environmental Engineering Research Center
6  Khalifa University, Department of Mechanical Engineering, Center for Catalysis and Separations

Abstract:

Ni/Al2O3 and Ni/CaO-MgO-Al2O3 catalysts were investigated for the biogas dry reforming reaction using CH4/CO2 mixtures with minimal dilution. Stability tests were conducted between 600 and 800 oC and TGA/DTG, Raman, STEM-HAADF, HR-TEM, XPS techniques were used to characterize the spent samples. Graphitized carbon allotrope structures, carbon nanotubes (CNTs) and amorphous carbon were formed on all samples. Metallic Ni0 was recorded for all (XPS), whereas a strong peak corresponding to Ni2O3/NiAl2O4 was observed for the Ni/Al2O3 sample (650–750°C). Stability tests confirmed that the Ni/CaO-MgO-Al2O3 catalyst deactivates at a more gradual rate and is more active and selective in comparison to the Ni/Al2O3 for all temperatures. The Ni/CaO-MgO-Al2O3 exhibits good durability in terms of conversion and selectivity, whereas the Ni/Al2O3 gradually loses its activity in CH4 and CO2 conversion, with a concomitant decrease of the H2 and CO yield. It can be concluded that doping Al2O3 with CaO-MgO enhances catalytic performance by: (a) maintaining the Ni0 phase during the reaction, due to higher dispersion and stronger active phase-support interactions, (b) leading to a less graphitic and more defective type of deposited carbon, and (c) facilitating the deposited carbon gasification due to the enhanced CO2 adsorption on its increased surface basic sites.

Keywords: biogas reforming reaction; syngas production; nickel catalysts; catalytic deactivation; carbon nanotubes; CaO-MgO doping
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