Stability of highly dispersed Ni/Al2O3 catalysts : Effects of pretreatment

Oxidic and reduced and passivated Al2O3-supported nickel catalysts with loading up to 19.3 wt% were characterized by temperature-programmed sulfiding (TPS), temperature-programmed reduction (TPR), and X-ray photoelectron spectroscopy. The oxidic catalyst precursors contain a highly disperse nickel species consisting of either an oxidic core and ahydroxide outer layer or a hydroxide as a whole, dependent on the Ni loading. The crystallite size of the active phase varies between 0.4 and 1.6 nm. This high dispersion was maintained during sulfidation. From TPR and TPS, it is inferred that no nickel aluminate is present. During reduction and passivation the crystallite size increases to 1.3–2.5 nm. From TPR of the oxidic catalyst it was concluded that the active phase contained more oxygen than that corresponding to the stoichiometry of NiO since an excess of hydrogen of 20–50% was consumed for the removal of the reactive oxygen species.

[1]  H. Yasuda,et al.  Hydrogenation of tetralin over sulfided nickel-tungstate/alumina and nickel-molybdate/alumina catalysts , 1997 .

[2]  J. Sueiras,et al.  Characterization of nickel species on several γ-alumina supported nickel samples , 1996 .

[3]  T. Yokoyama,et al.  Vibrational and anharmonic properties of the surface S-Ni bonds in c(2 × 2)S/Ni(100) and c(2 × 2)S/Ni(110) from the SEXAFS point of view , 1994 .

[4]  S. Smeds,et al.  Activation of Ni/A12O3 catalysts through modification of the Al2O3 support , 1994 .

[5]  J. Moulijn,et al.  Temperature-Programmed Reduction of Oxidic and Sulfidic Alumina-Supported NiO, WO3, and NiO-WO3 Catalysts , 1994 .

[6]  J. Moulijn,et al.  Comparison of the sulfiding rate and mechanism of supported NiO and Ni0 particles , 1992 .

[7]  D. Lide Handbook of Chemistry and Physics , 1992 .

[8]  J. Moulijn,et al.  Temperature-programmed reduction of NiOWO3/Al2O3 Hydrodesulphurization catalysts , 1989 .

[9]  J. Moulijn,et al.  Temperature-programmed reduction of CoOAI2O3 catalysts , 1985 .

[10]  J. Travert,et al.  Comparative adsorption of H2S, CH3SH and (CH3)2S on alumina. Structure of species and adsorption sites , 1981 .

[11]  J. Moulijn,et al.  Quantitative analysis of XPS intensities for supported catalysts , 1979 .

[12]  D. Hercules,et al.  Studies of nickel-tungsten-alumina catalysts by x-ray photoelectron spectroscopy , 1976 .

[13]  N. McIntyre,et al.  X‐Ray Photoelectron Spectroscopic Study of the Aqueous Oxidation of Monel‐400 , 1976 .

[14]  M. G. Cook,et al.  X-ray photoelectron studies on some oxides and hydroxides of cobalt, nickel, and copper , 1975 .

[15]  N. Winograd,et al.  X-ray photoelectron spectroscopic studies of nickel-oxygen surfaces using oxygen and argon ion-bombardment , 1974 .