Process for desulfurizing catalytically cracked gasoline

Details Process for desulfurizing catalytically cracked gasoline Process for desulfurizing catalytically cracked gasoline

C - Chemistry, Metallurgy

10

G

C10G 45/08 (2006.01)

Patent

CA 2184043

A catalytically cracked gasoline feedstock is desulfurized under reaction conditions of a hydrogen feed rate measured at the reactor inlet of from 1 to 5 mols per mol of the feedstock oil and of from 5 to 50 mols per mol of the olefin components contained in the feedstock oil, a reaction temperature of from 200 to 300°C, a total pressure inside the reactor of from 10 to 20 kg/cmG, and a liquid hourly space velocity of from 2 to 8 1/hr, and using a catalyst which comprises a support mainly comprising alumina and having a surface area of 200 m/g or larger, wherein MoO3 in an amount of from 10 to 20 wt% and CoO in an amount of from 3 to 6 wt% in terms of inner content are fixed to the support, and the weight ratio of MoO3 to CoO is from 2.5 to 4.5.

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