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U.S. Department of Energy
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Hydrofining of Athabasca derived heavy gas oil over Ni-W and Co-Mo catalysts

Conference ·
OSTI ID:5340798

The hydrotreatment of heavy gas oil derived from Athabasca bitumen was studied in a trickle bed reactor over Ni-W and Co-Mo zeolite catalyst at 350-425/sup 0/C, 3.55 to 10.44 MPa, and LHSV of 1-4. The effects of temperature and liquid flow rates on the product were investigated. ASTM distillation, aniline point, viscosities and densities of the product oil were measured and correlated with various parameters. Activity of the catalysts for hydrodenitrogenation is compared.

OSTI ID:
5340798
Report Number(s):
CONF-870822-
Country of Publication:
United States
Language:
English