In situ XPS investigations of Cu1−xNixZnAl-mixed metal oxide catalysts used in the oxidative steam reforming of bio-ethanol

• Published in: Applied catalysis. B, Environmental Environmental, 2005-02, Vol.55 (4), p.287-299
• Main Authors: Velu, Subramani, Suzuki, Kenzi, Vijayaraj, Munusamy, Barman, Sanmitra, Gopinath, Chinnakonda S.
• Format: Article
• Language: English
• Subjects: Auger electron spectroscopy; Autothermal reforming; Bio-ethanol; Copper oxide; Fuel cell; Hydrogen; Hydrotalcite; Mixed metal oxides; Nickel oxide; Oxidative steam reforming; Steam reforming; XPS
• ISSN: 0926-3373; 1873-3883
• DOI: 10.1016/j.apcatb.2004.09.007

A series of CuNiZnAl-multicomponent mixed metal oxide catalysts with various Cu/Ni ratios were prepared by the thermal decomposition of Cu1−xNixZnAl-hydrotalcite-like precursors and tested for oxidative steam reforming of bio-ethanol. Dehydrogenation of EtOH to CH3CHO is favored by Cu-rich catalyst. Introduction of Ni leads to CC bond rupture and producing CO, CO2 and CH4. H2 yield (selectivity) varied between 2.6–3.0mol/mol of ethanol converted (50–55%) for all catalysts at 300°C. The above catalysts were subjected to in situ XPS studies to understand the nature of active species involved in the catalytic reaction. Core level and valence band XPS as well as Auger electron spectroscopy revealed the existence of Cu2+, Ni2+ and Zn2+ ions on calcined materials. Upon in situ reduction at reactions temperatures, the Cu2+ was fully reduced to Cu0, while Ni2+ and Zn2+ were partially reduced to Ni0 and Zn0, respectively. On reduction, the nature of ZnO on Cu-rich catalyst changes from crystalline to amorphous, relatively inert and highly stabilized electronically. Relative concentration of the Ni0 and Zn0 increases upon reduction with decreasing Cu-content. Valence band results demonstrated that the overlap between 3d bands of Cu and Ni was marginal on calcined materials, and no overlap due to metallic clusters formation after reduction. Nonetheless, the density of states at Fermi level increases dramatically for Ni-rich catalysts and likely this influences the product selectivity.