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Competing reactions in hydrotreating coker distillates from Athabasca bitumen on unpromoted and promoted catalysts. [Comparison of unpromoted Mo oxide/alumina catalysts and promoted NiO--Mo oxide/alumina and CoO--Mo oxide/alumina catalysts]

Conference · · Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States)
OSTI ID:7119735

Desulfurization, denitrogenation, and hydrogenation reactions occur simultaneously in a hydrotreating process. Several unpromoted MoO/sub 3//alumina catalysts and promoted NiO--MoO/sub 3//alumina and CoO--MoO/sub 3//alumina catalysts were evaluated to compare the characteristics of these competing reactions. A coker kerosene distillate (193 to 279/sup 0/C) derived from Athabasca bitumen was used to evaluate the catalyst activity in the hydrotreating studies. The denitrogenation activity was higher than desulfurization activity for all MoO/sub 3//alumina catalysts. Promotion of MoO/sub 3//alumina catalysts with nickel or cobalt selectively improved desulfurization so that the extent of the various reactions decreased in the following order: desulfurization greater than denitrogenation greater than aromatic hydrogenation. The interactions of denitrogenation and desulfurization reactions at various temperatures were compared for promoted and unpromoted catalysts. The results obtained by others for hydrotreating gas oil and low temperature tar were also compared. The conversions and the interaction of desulfurization and denitrogenation reactions were found to be dependent on the type of catalyst, temperature of reaction and boiling range of the feedstock.

Research Organization:
Energy Research Labs., Ottawa, Ontario
OSTI ID:
7119735
Journal Information:
Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States), Journal Name: Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States) Vol. 21:6; ISSN ACFPA
Country of Publication:
United States
Language:
English