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Hydrocracking of gas oil using USY-zeolite-based catalyst

Alsobaai, Ahmed Mubarak and Bassim, H. Hameed and Ridzuan, Zakaria (2006) Hydrocracking of gas oil using USY-zeolite-based catalyst. In: 1st International Conference on Natural Resources Engineering & Technology 2006, 24-25th July 2006, Putrajaya, Malaysia.

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The conversion of petroleum gas oil to transportation fuels was investigated using NiMo, CoMo, NiW and CoW catalysts supported on commercial USY zeolite. The catalysts were prepared using the incipient wetness method. The reaction was carried out in a high-pressure shaking reactor at reaction temperature of 450 oC, contact time of 90 minutes and catalyst to sample ratio of 0.04. It was found that over NiW/USY catalyst, the values of total conversion and yield of total distillate fuels were 64.35 and 54.12 wt%, respectively, compared to 46.48 and 38.25 wt% over unloaded USY zeolite. The hydrocracking activities of other USY-based catalysts were increased as follows, from most active to least active: NiW/USY> NiMo/USY> CoW/USY > CoMo/USY > USY. The catalysts were characterized by TGATPD acidity, TGA thermal stability, and BET surface-area measurements.

Item Type:Conference or Workshop Item (Paper)
Uncontrolled Keywords:Petroleum gas oil; USY-based catalyst; high-pressure shaking reactor.
Subjects:T Technology > TP Chemical technology
Divisions:Chemical and Natural Resources Engineering (Formerly known)
ID Code:268
Deposited By: Rasyidah Mohd Daud
Deposited On:15 Feb 2007 10:59
Last Modified:23 Aug 2017 07:10

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