Mineral oils: processes and products – Refining – Sulfur removal
Patent
1996-08-23
1998-12-29
Myers, Helane
Mineral oils: processes and products
Refining
Sulfur removal
208217, 208216R, 208243, 208244, 208 58, 208 97, C10G 4560
Patent
active
058535705
ABSTRACT:
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.degree. to 300.degree. C., a total pressure inside the reactor of from 10 to 20 kg/cm.sup.2 G, and a liquid hourly space velocity of from 2 to 8 l/hr, and using a catalyst which comprises a support mainly comprising alumina and having a surface area of 200 m.sup.2 /g or larger, wherein MoO.sub.3 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 MoO.sub.3 to CoO is from 2.5 to 4.5.
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Hatanaka Shigeto
Hikita Satoru
Miyama Tadao
Sadakane Osamu
Mitsubishi Oil Co., Ltd.
Myers Helane
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