Dinitrogenation of mineral oil utilizing a fluorine-promoted, alumina-supported metal catalyst

Claim 2

A process for the denitrogenation of a mineral oil feedstock, which comprises contacting said feedstock in admixture with added hydrogen at elevated denitrogenation temperatures and pressures with a catalyst consisting essentially of a sulfided alumina-supported composite of a first component of molybdenum and/or tungsten, a second component of nickel and/or cobalt and a fluorine component, said second component and said fluorine component having been incorporated into said catalyst by a single impregnation procedure including the steps of: (1) forming porous cohesive aggregates comprising said alumina support in the form of calcined gamma alumina; (2) impregnating said aggregates with an aqueous impregnation solution having dissolved therein one or more fluosilicate salts of cobalt and/or nickel; and (3) drying and calcining the impregnated aggregates from step (2).

Claim 3

A process as described in claim 1 wherein said impregnation in step (2) is carried out by uniformly applying to said aggregates an amount of said impregnation solution sufficient to saturate at least about 90% of the pore volume of said aggregates, but not substantially in excess of the amount required for 100% saturation thereof.

Claim 4

A process as defined in claim 1 wherein said aggregates from step (1) also comprise said first component intimately composited therein in calcined form.

Claim 5

A process as defined in claim 1 wherein said first component is incorporated into said catalyst by including in said impregnation solution in step (2) a soluble form of said first component.

Claim 6

A process as defined in claim 1 wherein said first component is incorporated into said catalyst by impregnation following step (3).

Claim 7

A process as defined in claim 1 wherein said first component is molybdenum and said second component is nickel.

Claim 8

A process for the denitrogenation of a mineral oil feedstock, which comprises contacting said feedstock in admixture with added hydrogen at elevated denitrogenation temperatures and pressures with a catalyst consisting essentially of a sulfided alumina-supported composite of a first component of molybdenum and/or tungsten, a second component of nickel and/or cobalt and a fluorine component, said second component and said fluorine component having been incorporated into said catalyst by a single impregnation procedure including the steps of: (1) forming porous cohesive aggregates comprising said alumina support in the form of calcined gamma alumina; (2) forming an aqueous impregnation solution having dissolved therein a sufficient concentration of soluble precursors of said fluorine component and said second component to provide, in a volume of said solution equal to the total pore volume of said aggregates to be impregnated, the total amount of said fluorine component and said second component desired in the finished catalyst, at least the major atomic portions of F, Co and Ni in said solution being in the form of cobalt and/or nickel fluosilicate; (3) uniformly applying to said aggregates an amount of said impregnation solution sufficient to saturate at least about 90% of the pore volume of said aggregates but not substantially in excess of the amount required for 100% saturation thereof, and (4) drying and calcining the aggregates from step (3).

Claim 9

A process for the denitrogenation of a mineral oil feedstock, which comprises contacting said feedstock in admixture with added hydrogen at elevated denitrogenation temperatures and pressures with a catalyst consisting essentially of a sulfided alumina-supported composite of a first component of molybdenum and/or tungsten, a second component of nickel and/or cobalt and a fluorine component, said second component and said fluorine component having been incorporated into said catalyst by a single impregnation procedure including the steps of: (1) forming porous cohesive aggregates comprising said alumina support in the form of calcined gamma alumina; (2) forming an aqueous impregnation solution having dissolved therein a sufficient concentration of soluble precursors of said fluorine component and said second component to provide, in a volume of said solution equal to the total pore volume of said aggregates to be impregnated, the total amount of said fluorine component and said second component desired in the finished catalyst, at least the major atomic portions of F, Co and Ni in said solution being in the form of cobalt and/or nickel fluosilicate; (3) uniformly applying to said aggregates an amount of said impregnation solution sufficient to saturate at least about 90% of the pore volume of said aggregates but not substantially in excess of the amount required for 100% saturation thereof, and (4) drying and calcining the aggregates from step (3).

Claim 10

A process as defined in claim 1 wherein said aggregates from step (1) also comprise said first component intimately composited therein in calcined form.

Claim 11

A process as defined in claim 1 wherein said first component is incorporated into said catalyst by including in said impregnation solution in step (2) a soluble form of said first component.

Claim 12

A process as defined in claim 1 wherein said first component is incorporated into said catalyst by impregnation following step (4).

Claim 13

A process as defined in claim 1 wherein said first component is molybdenum and said second component is nickel.