Catalyst for the selective hydrogenation of polyunsaturated organics
AssigneeUop LLC
InventorsMark J. Gattuso, Daniel L. Ellig
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AssigneeUop LLC
InventorsMark J. Gattuso, Daniel L. Ellig
Estimating the term…
A process is presented which is useful for the selective hydrogenation of polyunsaturated organic compounds. The resultant product of such a reaction produces the monoolefinic equivalents of the hydrogenated polyunsaturated organic compounds. The catalyst used in this selective hydrogenation process comprises nickel and sulfur deposited on the surface of an alumina support. The preferred catalyst does not contain halogens, noble metals, alkaline earth metals, or alkali metals and is characterized by having only a very low percentage of the total pore volume being provided by pores having an average pore diameter less than 150 angstroms. The great majority of the pore volume is present in the form of macropores having diameters of 500 to 1500 angstroms.
A process for the selective hydrogenation of polyunsaturated organic compounds to monoolefinic organic compounds comprising contacting a feed comprising at least one organic compound selected from the group consisting of dienes, polyenes, alKynes, and triple bonded nitriles in a reaction zone at selective hydrogenation conditions with a catalyst consisting essentially of an alumina support material, about 0.05 to 1.5 wt. % sulfur, and about 1.0 to 25.0 wt. % nickel, where the alumina support material is characterized by having a total pore volume greater than 1.4 but less than 2.5 cc/g, a surface area greater than 150 m.sup.2 /g, with less than 25 percent of the total pore volume being provided by pores having pore diameters of less than 150 angstroms and with over 60 percent of the pore volume being provided by pores having pore diameters greater than 600 angstroms to produce a product substantially free of polyunsaturated organic compounds.
Dependencies are inferred from the claim text.