Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
134 words
Method for the preparation of insulating oil having good oxidation stability, electric characteristics and resistance to copper corrosion which comprises subjecting a distillate within a temperature having a boiling range from 250° to 400° C. at atmospheric pressure to solvent refining to provide a raffinate oil in which 30 to 75% by weight of the sulfur present in the distillate is removed in said solvent refining step, said distillate having been obtained from a paraffin base crude oil or mixture base crude oil, subjecting said raffinate to hydrogenating refining with hydrogen and a hydrogenation catalyst to reduce from 40 to 90% by weight of the sulfur present in the raffinate and subjecting said hydrogenated oil to solvent dewaxing to provide said insulating oil having a sulfur content from 0.1 to 0.35 percent by weight.
Claim 2
Dependent Claim
134 words
Method for the preparation of insulating oil having good oxidation stability, electric characteristics and resistance to copper corrosion which comprises subjecting a distillate within a temperature having a boiling range from 250° to 400° C. at atmospheric pressure to solvent refining to provide a raffinate oil in which 30 to 75% by weight of the sulfur present in the distillate is removed in said solvent refining step, said distillate having been obtained from a paraffin base crude oil or mixture base crude oil, subjecting said raffinate to hydrogenating refining with hydrogen and a hydrogenation catalyst to reduce from 40 to 90% by weight of the sulfur present in the raffinate and subjecting said hydrogenated oil to solvent dewaxing to provide said insulating oil having a sulfur content from 0.1 to 0.35 percent by weight.
Claim 3
Dependent Claim
28 words
Method according to claim 1 wherein the solvent used for the solvent refining is one member selected from the group consisting of furfural, liquid sulfur dioxide and phenol.
Claim 4
Dependent Claim
79 words
Method according to claim 1 wherein the hydrogenating refining of the raffinate is carried out at a temperature from 230° to 350° C. under a pressure from 25 to 100 kg./cm. 2 using as the catalyst oxides of at least one metal selected from the group consisting of metals of Groups VI, IB and VIII in the Periodic Table on a carrier selected from the group consisting of bauxite, active carbon, fuller's earth, diatomaceous earth, zeolite, silica and silica-alumina.
Claim 5
Dependent Claim
25 words
Method according to claim 1 wherein the solvent used for the solvent dewaxing is a benzene-toluene-acetone solvent mixture or a benzene-toluene-methyl ethyl ketone solvent mixture.
Claim 6
Dependent Claim
35 words
Method according to claim 1 wherein the clay treatment is carried out with active clay at a temperature from 60° to 80° C. for a contact period of time from 30 minutes to 1 hour.
Claim 7
Dependent Claim
31 words
The method of claim 1, wherein the dewaxed product is subjected to a clay treatment to provide a final product having a sulfur content of from 0.1 to 0.35% by weight.