Mo-promoted Ni/Al2O3 catalyst for dry reforming of methane

• Published in: International journal of hydrogen energy 2017-09, Vol.42 (37), p.23500-23507
• Main Authors: Yao, Lu, Galvez, Maria Elena, Hu, Changwei, Da Costa, Patrick
• Format: Article
• Language: English
• Subjects: Carbon dioxide; Hydrogen production; Methane; Molybdenum; Nickel catalysts
• ISSN: 0360-3199; 1879-3487
• DOI: 10.1016/j.ijhydene.2017.03.208

Mo-promoted alumina supported Ni catalysts were prepared through a conventional impregnation method and tested in dry reforming of methane (DRM) at temperatures from 550 to 850 °C. The catalysts were characterized by means of H2-temperature programmed reduction (H2-TPR), CO2-temperature programmed desorption (CO2-TPD), X-ray diffraction (XRD), N2 physisorption and Raman spectroscopy. Mo-promotion caused a reduction in the DRM catalytic activity. The weaker interaction between NiO species and the alumina support, the formation of a MoNi4 phase, and the lower basicity of this Ni-Mo/Al2O3 catalyst were identified as the main causes for its lower activity. However, pre-reducing the Ni-Mo/Al2O3 catalyst at temperatures lower than 700 °C, instead of 900 °C, resulted in a considerable increase of its catalytic activity. This was mainly due to the formation of a separate Ni0 phase that did not interact with Mo and to an increase in medium strength basicity. [Display omitted] •Ni-Mo/Al2O3 catalyst exhibited lower activity than that of Ni/Al2O3 catalyst.•The NiMoO4 species was formed over calcined Ni-Mo/Al2O3 catalyst.•MoNi4 phase was formed upon reduction of NiMoO4 species at 900 °C.•Ni-Mo/Al2O3 showed low basicity and weak interaction between NiO and Al2O3.•Lowering reduction temperature could improve the activity of Ni-Mo/Al2O3.