Hydrogenation process employing a zinc promoted catalyst

Claim 2

A process which comprises contacting a hydrocarbon feed selected from the group consisting of naphtha and heavier liquid hydrocarbons with a catalyst in a hydrogenation zone under hydrogenation conditions to separate sulfur and nitrogen from said hydrocarbon feed, said catalyst consisting essentially of a Group VI-B metal, nickel and zinc supported on alumina or a silica-stabilized alumina, the Group VI-B metal and nickel being in the sulfided form, and recovering a hydrogenated hydrocarbon product from said hydrogenation zone.

Claim 3

The process of claim 1 wherein said Group VI-B metal comprises molybdenum.

Claim 4

The process of claim 1 wherein said hydrogenation conditions include a temperature in the range from about 500° to about 1,000° F., a pressure in the range from about 100 to about 10,000 psig, a hydrogen feed rate in the range of about 500 to about 10,000 standard cubic feet per barrel of hydrocarbon feed, and a space velocity in the range from about 0.10 to about 10.0 volumes of feed stock per volume of catalyst per hour.

Claim 5

The process of claim 3 wherein the concentration of zinc is in the range between 0.25 and about 5.0 weight percent of said catalyst.

Claim 6

The process of claim 1 wherein said hydrogenation conditions include a pressure in the range of 200 to 3,500 psig, a liquid hourly space velocity in the range of 0.3 to 5.0, a temperature in the range of 550° to 800° F., and hydrogen circulation rate in the range of 1,000 to 8,000 standard cubic feet per barrel of hydrocarbon feed, and wherein the hydrogenated product recovered from said hydrogenation zone contains substantially less nitrogen.

Claim 7

The process of claim 1 wherein said hydrocarbon feed comprises naphtha and said hydrogenation conditions include a pressure in the range of 100 to 400 psig, a temperature in the range of 550° to 700° F., a liquid hourly space velocity in the range of 4.0 to 8.0, and a hydrogen circulation rate in the range of 1,000 to 2,000 standard cubic feet per barrel of hydrocarbon feed.

Claim 8

A process for the hydrodesulfurization of a sulfur-containing gas oil feed which comprises contacting said gas oil with hydrogen and a catalyst consisting essentially of a Group VI-B metal and nickel supported on alumina, said catalyst being promoted with from about 0.25 to about 5 weight percent of zinc, said Group VI-B metal and nickel being in the sulfided form, said contacting being conducted at a temperature from about 600° F. to about 780° F., at a pressure from about 400 to about 1500 psig, at a liquid hourly space velocity from about 0.7 to about 5.0 volumes of the gas oil feed per volume of catalyst per hour and at a hydrogen feed rate from about 500 to about 2,000 standard cubic feet of hydrogen per barrel of gas oil feed, and recovering therefrom a desulfurized gas oil product.

Claim 9

A process for the hydrodesulfurization of a sulfur-containing gas oil feed which comprises contacting said gas oil with hydrogen and a catalyst consisting essentially of a Group VI-B metal and nickel supported on alumina, said catalyst being promoted with from about 0.25 to about 5 weight percent of zinc, said Group VI-B metal and nickel being in the sulfided form, said contacting being conducted at a temperature from about 600° F. to about 780° F., at a pressure from about 400 to about 1500 psig, at a liquid hourly space velocity from about 0.7 to about 5.0 volumes of the gas oil feed per volume of catalyst per hour and at a hydrogen feed rate from about 500 to about 2,000 standard cubic feet of hydrogen per barrel of gas oil feed, and recovering therefrom a desulfurized gas oil product.

Claim 10

A process for the hydrodesulfurization of a sulfur-containing residual hydrocarbon feed which comprises contacting said residual hydrocarbon feed with hydrogen and a catalyst consisting essentially of a Group VI-B metal and nickel, the Group VI-B metal and nickel being in the sulfided form, supported on alumina, said catalyst being promoted with from about 0.65 to about 5 weight percent of zinc, said contacting being conducted at a temperature in the range of 600° to 800° F., at a pressure from about 500 to 2,500 psig, at a liquid hourly space velocity from about 0.3 to about 5 volumes of residual hydrocarbon feed per volume of catalyst per hour and at a hydrogen circulation rate from about 1,000 to about 8,000 standard cubic feet of hydrogen per barrel of residual hydrocarbon feed, and recovering therefrom a desulfurized residual hydrocarbon product.

Claim 11

A process for the hydrodesulfurization of a sulfur-containing residual hydrocarbon feed which comprises contacting said residual hydrocarbon feed with hydrogen and a catalyst consisting essentially of a Group VI-B metal and nickel, the Group VI-B metal and nickel being in the sulfided form, supported on alumina, said catalyst being promoted with from about 0.65 to about 5 weight percent of zinc, said contacting being conducted at a temperature in the range of 600° to 800° F., at a pressure from about 500 to 2,500 psig, at a liquid hourly space velocity from about 0.3 to about 5 volumes of residual hydrocarbon feed per volume of catalyst per hour and at a hydrogen circulation rate from about 1,000 to about 8,000 standard cubic feet of hydrogen per barrel of residual hydrocarbon feed, and recovering therefrom a desulfurized residual hydrocarbon product.