Demetalation and desulfurization of residual oil utilizing hydrogen and trickle beds of catalysts in three zones
AssigneeMobil Oil Corporation
InventorsDonald Milstein, Ronald H. Fischer
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AssigneeMobil Oil Corporation
InventorsDonald Milstein, Ronald H. Fischer
Estimating the term…
This invention is concerned with removing metal and sulfur contaminants from residual oil fractions by catalytic contact with two different catalysts in the presence of hydrogen. In this process, the oil is first contacted with the major fraction of a catalyst comprising a Group VIB metal and an iron group metal oxide, such as a mixture of cobalt and molybdenum oxides, composited with an alumina support, the catalyst having at least 60% of its pore volume in pores of 100A to 200A diameter and at least about 5% of its pore volume in pores having a diameter greater than 500A. The oil is then contacted with a secondcatalyst of the high surface-area, cobalt-molybdenum on alumina type having a major fraction of its pores in the 30 to 100A diameter range. Finally, the oil is contacted with the remainder of the large-pore catalyst.
A method for demetalizing and desulfurizing a residual oil which comprises passing a mixture of hydrogen and said oil at a hydrogen pressure of 500 to 3000 psig, a temperature of about 600 .degree.to 850.degree. F, and a space velocity of 0.1 to 5.0 LHSV, through trickle beds of catalysts disposed in three sequential reaction zones, the first zone containing a relatively larger bed of a said first catalyst, the third zone containing a relatively smaller bed of said first catalyst, and the second zone located between said first zone and said third zone containing a second catalyst, said first catalyst and said second catalyst comprising the oxides or sulfides of a Group VIB metal and an iron group metal on an alumina support, said first catalyst having at least 60 percent of its pore volume in pores with diameters of about 100 to 200A and at least about 5 percent of its pore volume in pores greater than 500A diameter, and said second catalyst having a surface area of at least 150 m.sup.2 /g and at least 50 percent of its pore volume in pores with diameters of 30 to 100A.
Dependencies are inferred from the claim text.