Abstract

Abstract The structure and catalytic properties of the supported Ni/γ-Al 2 O 3 catalyst prepared with different nickel salt precursors for hydrogenation of a-pinene have been studied using X-ray diffraction, UV–VIS diffuse reflectance spectroscopy, temperature-programmed reduction, CO chemisorption, and microreactor tests. It has been shown that the catalytic hydrogenation activity of the Ni/γ-Al 2 O 3 catalyst increases with increasing Ni loading, and the catalytic activity of the nickel acetate-derived Ni/γ-Al 2 O 3 catalyst is much higher than that of the nickel nitrate-derived catalyst. The catalyst characterization results indicate that the different catalytic hydrogenation activity of Ni/γ-Al 2 O 3 prepared with different nickel salt precursors is correlated to the different ratio of Ni 2+ ions in the tetrahedral and octahedral vacancies of γ-Al 2 O 3 and the different reduction degree of the NiO/γ-Al 2 O 3 precursors. When the nickel ion loading is far below the dispersion capacity, the supported nickel ions preferentially incorporate into the tetrahedral vacancies of γ-Al 2 O 3 . With increasing nickel loading, the ratio of Ni 2+ ions that incorporate into the octahedral vacancies of γ-Al 2 O 3 increases. The dispersion capacity of nickel ions on γ-Al 2 O 3 derived from nickel acetate is lower than that of the sample derived from nickel nitrate due to the greater shielding effect of acetate anions than nitrate anions. Moreover, the ratio of octahedral Ni 2+ to tetrahedral Ni 2+ on the nickel acetate-derived sample is higher than that on the nickel nitrate-derived sample because of the lower density of octahedral vacancies on γ-Al 2 O 3 . As octahedral Ni 2+ ions are easier to be reduced to the metallic state than tetrahedral Ni 2+ ions, the catalytic activity of the Ni/γ-Al 2 O 3 catalyst prepared with the nickel acetate precursor is much higher than that of the catalyst prepared with the nickel nitrate precursor with the same nickel loading.

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