Hydrocracking process and catalyst for production of middle distillate oils

Claim 2

A process for hydrocracking a mineral oil feedstock boiling predominantly above about 700° F to produce a middle distillate product boiling in the range of about 300°-700° F, which comprises contacting said feedstock plus added hydrogen, and under hydrocracking conditions, with a catalyst comprising a molybdenum and/or tungsten first component plus a nickel and/or cobalt second component supported on a heterogeneous support consisting essentially of about 10-50 weight-percent of a finely divided cracking component dispersed in an alumina matrix, said cracking component being a silica-alumina cogel or copolymer containing about 50-96 weight-percent SiO 2 , said hydrocracking conditions being correlated so as to give at least about 50 volume percent conversion of feedstock boiling above 700° F to liquid products boiling below 700° F.

Claim 3

A process as defined in claim 1 wherein at least about 75 volume-percent of said liquid products boiling below 700° F comprises said middle distillate product.

Claim 4

A process as defined in claim 1 wherein said first component is tungsten, or an oxide or sulfide thereof, and said second component is nickel or an oxide or sulfide thereof.

Claim 5

A process as defined in claim 3 wherein at least about 75 volume-percent of said liquid products boiling below 700° F comprises said middle distillate product.

Claim 6

A process as defined in claim 1 wherein said cracking component contains about 50-90 weight-percent SiO 2 .

Claim 7

A process for hydrocracking a mineral oil feedstock boiling predominantly above about 700° F to produce a middle distillate product boiling in the range of about 300°-700° F, which comprises contacting said feedstock plus added hydrogen, and under hydrocracking conditions, including a space velocity above about 0.5, with a catalyst comprising a minor proportion of tungsten or an oxide or sulfide thereof plus a minor proportion of nickel or an oxide or sulfide thereof supported on a heterogeneous support consisting essentially of about 10-50 weight-percent of a finely divided cracking component dispersed in an alumina matrix, said cracking component being a silica-alumina cogel or copolymer containing about 50-96 weight-percent SiO 2 , said hydrocracking conditions being correlated so as to give at least about 60 volume percent conversion of feedstock boiling above 700° F to liquid products boiling below 700° F, at least about 75 volume-percent of said liquid products boiling below 700° F comprising said middle distillate product.

Claim 8

A process for hydrocracking a mineral oil feedstock boiling predominantly above about 700° F to produce a middle distillate product boiling in the range of about 300°-700° F, which comprises contacting said feedstock plus added hydrogen, and under hydrocracking conditions, including a space velocity above about 0.5, with a catalyst comprising a minor proportion of tungsten or an oxide or sulfide thereof plus a minor proportion of nickel or an oxide or sulfide thereof supported on a heterogeneous support consisting essentially of about 10-50 weight-percent of a finely divided cracking component dispersed in an alumina matrix, said cracking component being a silica-alumina cogel or copolymer containing about 50-96 weight-percent SiO 2 , said hydrocracking conditions being correlated so as to give at least about 60 volume percent conversion of feedstock boiling above 700° F to liquid products boiling below 700° F, at least about 75 volume-percent of said liquid products boiling below 700° F comprising said middle distillate product.

Claim 9

A process as defined in claim 6 wherein at least about 80 volume-percent of said liquid products boiling below 700° F comprises said middle distillate product.

Claim 10

A process as defined in claim 6 wherein said hydrocracking is carried out at about 600°-800° F and about 1000-3000 psig, and wherein said feedstock contains substantial proportions of organic nitrogen and sulfur compounds.