Abstract A process for making technical white oils in a single step hydrogenation and without the need for acid treating to meet white oil specification by hydrogenating a hydrocracked solvent extracted lubricating oil distilling between 650° and 1050° F., having a SUS/100° F. viscosity of about 200 and an aromatic content of less than about 15% in a single step at 600° to 700° F., and at 2000 to 3000 psig in the presence of a catalyst comprising nickel and tungsten supported on silica-alumina, subjecting the hydrogenated solvent extracted lube oil to atmospheric distillation to remove distillates useful as fuels and subjecting the bottoms of said atmospheric distillation to a vacuum distillation to yield various viscosity grades of technical white oils.
A process for making technical white oils in a single hydrogenation and without the need for acid treating to meet white oil specifications which comprises hydrogenating a hydrocracked solvent extracted lubricating oil distilling at 650° to 1050° F, having a SUS/100° F viscosity of about 200 and an aromatic content of less than about 15% in a single step at 600° to 700° F, and at 2000 to 3000 psig in the presence of a catalyst comprising nickel and tungsten supported on silica-alumina, subjecting the hydrogenated solvent lube oil to atmospheric distillation to remove distillates useful as fuels and subjecting the bottoms of said atmospheric distillation to a vacuum distillation to yield technical white oils as products.
Claim 2
Dependent Claim
117 words
A process for making technical white oils in a single hydrogenation and without the need for acid treating to meet white oil specifications which comprises hydrogenating a hydrocracked solvent extracted lubricating oil distilling at 650° to 1050° F, having a SUS/100° F viscosity of about 200 and an aromatic content of less than about 15% in a single step at 600° to 700° F, and at 2000 to 3000 psig in the presence of a catalyst comprising nickel and tungsten supported on silica-alumina, subjecting the hydrogenated solvent lube oil to atmospheric distillation to remove distillates useful as fuels and subjecting the bottoms of said atmospheric distillation to a vacuum distillation to yield technical white oils as products.
Claim 3
Dependent Claim
83 words
The process of claim 1 where the charge stock is a mixture of about 40% by volume of a furfural extracted dearomatized vacuum gas oil and about 60% of a virgin vacuum gas oil which is refined by hydrocracking into a lube quality oil having a high VI of about 95 to 105 and an aromatic content of about 10% to about 15% by volume, and the portion boiling above 650° F is solvent dewaxed and U.V. stabilized with a light furfural extraction.
Claim 4
Dependent Claim
65 words
The process of claim 1 where the charge stock is a 100% virgin vacuum gas oil which is refined by hydrocracking into a lube quality oil having a high VI of about 95 to 105 and an aromatic content of about 10% to about 15% by volume, and the portion boiling above 650° F is solvent dewaxed and U.V. stabilized with a light furfural extraction.