Effect of Calcination Temperature on the Structure and Catalytic Performance of the Ni/Al2O3 and Ni–Ce/Al2O3 Catalysts in Oxidative Dehydrogenation of Ethane

We studied the effect of calcination temperature of Ni/Al 2 O 3 and Ni–Ce/Al 2 O 3 catalysts on the specific surface area, acidity, ratio of pore volume and specific surface area, reducibility reflecting the changing population of Ni(T d ) and Ni(O h ) species, and activity/selectivity in oxidative dehydrogenation of ethane. It should be stressed that the role of Ce as a promoter on the catalytic activity of Ni–Ce/Al 2 O 3 catalysts decreased with an increasing value of the calcination temperature. At a reaction temperature of 500 °C, the highest productivity to ethene was observed for the Ni–Ce/Al 2 O 3 catalyst calcined at 500 °C. Ni–Ce/Al 2 O 3 catalysts calcined at 500–750 °C showed the same selectivity to ethene. The Ni–Ce/Al 2 O 3 catalysts calcined at 900 and 1000 °C showed a sharp decrease in the selectivity and the activity, which was probably associated with the formation of NiAl 2 O 4 spinel.