Hydrocracking of petroleum heavy oils using transition metal-loaded zeolite
catalyst was examined. Deasphalted oil (DAO) derived from vacuum residue o
f a mixture of Arabian light and medium crudes was successfully converted t
o gasoline fraction, attaining yield of more than 70%, using palladium and
nickel co-loaded Y-type zeolite catalyst, at 350 degrees C for 1 h, in H-2
pressurized to 4.9 MPa. The mechanism of this hydrocracking process is disc
ussed briefly. The authors also tried hydrocracking of fraction heavier tha
n DAO, i.e, maltene, this affording gaseous products (C-2-C-4) and gasoline
fraction, 35% and 52%, respectively, under the following conditions: 400 d
egrees C, for 3 h, in H-2 pressurized to 6.9 MPa, over the same catalyst.