Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
252 words
A process for preparing a lubricating oil concentrate of a viscosity index improver having sludge dispersing properties and a number average molecular weight in the range of about 10,000 to 250,000; comprising dissolving from 5 to 30 weight percent of ethylene copolymer comprising 30 to 80 wt. % ethylene and 20 to 70 wt. % C 3 to C 18 alpha-olefin in a mineral lubricating oil as solvent, maintaining said resulting copolymer-oil solution at a temperature of from about 100° C. to about 250° C. and under an inert atmosphere while admixing an ethylenically-unsaturated dicarboxylic acid material selected from the group consisting of maleic anhydride, maleic anhydride derivatives, maleic acid and fumaric acid, and a free-radical initiator having a boiling point in excess of about 100° C. into said solution, wherein the weight ratio of said dicarboxylic acid material to said initiator is about 1:1 to 30:1, and maintaining said temperature and inert atmosphere for about 0.1 to 12 hours to graft said acid material onto said ethylene copolymer and said solvent, without substantial molecular weight breakdown of said ethylene copolymer, and thereafter reacting carboxy groups of said grafted polymer with a polyfunctional material selected from the group consisting of polyamines having 3 to 20 carbon atoms and 2 to 12 nitrogen atoms, C 2 to C 30 polyols having 2 to 10 hydroxyl radicals, and C 2 to C 30 hydroxy amines having 1 to 6 hydroxy groups and 1 to 10 nitrogen atoms, to thereby form said lubricating oil concentrate.
Claim 2
Dependent Claim
252 words
A process for preparing a lubricating oil concentrate of a viscosity index improver having sludge dispersing properties and a number average molecular weight in the range of about 10,000 to 250,000; comprising dissolving from 5 to 30 weight percent of ethylene copolymer comprising 30 to 80 wt. % ethylene and 20 to 70 wt. % C 3 to C 18 alpha-olefin in a mineral lubricating oil as solvent, maintaining said resulting copolymer-oil solution at a temperature of from about 100° C. to about 250° C. and under an inert atmosphere while admixing an ethylenically-unsaturated dicarboxylic acid material selected from the group consisting of maleic anhydride, maleic anhydride derivatives, maleic acid and fumaric acid, and a free-radical initiator having a boiling point in excess of about 100° C. into said solution, wherein the weight ratio of said dicarboxylic acid material to said initiator is about 1:1 to 30:1, and maintaining said temperature and inert atmosphere for about 0.1 to 12 hours to graft said acid material onto said ethylene copolymer and said solvent, without substantial molecular weight breakdown of said ethylene copolymer, and thereafter reacting carboxy groups of said grafted polymer with a polyfunctional material selected from the group consisting of polyamines having 3 to 20 carbon atoms and 2 to 12 nitrogen atoms, C 2 to C 30 polyols having 2 to 10 hydroxyl radicals, and C 2 to C 30 hydroxy amines having 1 to 6 hydroxy groups and 1 to 10 nitrogen atoms, to thereby form said lubricating oil concentrate.
Claim 3
Dependent Claim
24 words
A process according to claim 1, wherein said C 3 to C 18 alpha-olefin is propylene and said dicarboxylic acid material is maleic anhydride.
Claim 4
Dependent Claim
13 words
A process according to claim 2, wherein said polyfunctional material is said polyamine.
Claim 5
Dependent Claim
13 words
A process according to claim 2, wherein said polyfunctional material is a polyol.
Claim 6
Dependent Claim
14 words
A process according to claim 2, wherein said polyfunctional material is a hydroxy amine.
Claim 7
Dependent Claim
12 words
A process according to claim 1, wherein said initiator is a peroxide.
Claim 8
Dependent Claim
35 words
A process according to claim 6, wherein said initiator is 2,5-dimethyl-hex-3-yne-2,5-bis-tertiary-butyl peroxide and is used in a concentration of from about 0.005 to 1 wt. %, based upon the total weight of said copolymer-oil solution.
Claim 9
Dependent Claim
19 words
A process according to claim 7, wherein said grafting temperature is in the range of 120° to 190° C.
Claim 10
Dependent Claim
26 words
A process according to claim 8, wherein the weight ratio of said dicarboxylic acid material to said initiator is within the range of 2.0:1 to 5.0:1.
Claim 11
Dependent Claim
11 words
The lubricating oil concentrate produced by the process of claim 1.
Claim 12
Dependent Claim
11 words
The lubricating oil concentrate produced by the process of claim 3.
Claim 13
Dependent Claim
11 words
The lubricating oil concentrate produced by the process of claim 4.
Claim 14
Dependent Claim
11 words
The lubricating oil concentrate produced by the process of claim 5.
Claim 15
Dependent Claim
23 words
A lubricating oil composition comprising a major proportion of lubricating oil and a minor V.I. improving amount of the concentrate of claim 10.
Claim 16
Dependent Claim
23 words
A lubricating oil composition comprising a major proportion of lubricating oil and a minor V.I. improving amount of the concentrate of claim 11.
Claim 17
Dependent Claim
23 words
A lubricating oil composition comprising a major proportion of lubricating oil and a minor V.I. improving amount of the concentrate of claim 12.
Claim 18
Dependent Claim
23 words
A lubricating oil composition comprising a major proportion of lubricating oil and a minor V.I. improving amount of the concentrate of claim 13.