Claims
- 1. A process for preparing a nitrogen containing copolymer comprising reacting, in the presence of a free radical initiator,
(A) from about 55% to about 99.9% by weight of one or more alkyl acrylate ester monomers containing from 1 to about 24 carbon atoms in the ester alkyl group, wherein at least about 50 mole % of the esters contain at least 6 carbon atoms in the ester alkyl group, and (B)from about 0.1% to about 45% by weight of at least one nitrogen containing monomer selected from the group consisting of vinyl substituted nitrogen heterocyclic monomers, dialkylaminoalkyl acrylate monomers, dialkylaminoalkyl acrylamide monomers, N-tertiary alkyl acrylamides, and vinyl substituted amines provided that the total of (A) and (B) equals 100%, and optionally, in the presence of a chain transfer agent, wherein monomer (A), the free radical initiator, and if used, the chain transfer agent, are first combined to form a mixture, whereupon from about 10% to about 80% of said mixture is mixed with monomer (B); from about 20% to about 100% of the mixture of monomers (A) and (B) is heated until an exotherm is noted, then while maintaining reaction temperature, first adding the balance, if any, of the mixture of monomers (A) and (B) over about 0.25 hour to about 5 hours followed by addition over 0.25 to about 5 hours of the remaining mixture of monomer (A) and initiator, optionally adding additional initiator, whereupon the reaction is continued to completion.
- 2. The process of claim 1 wherein from about 20% to about 80% of the mixture of monomers (A) and (B) is heated until the exotherm is noted.
- 3. The process of claim 1 wherein 100% of the mixture of monomers (A) and (B) is heated until the exotherrn is noted.
- 4. The process of claim 1 wherein at least about 50 mole % of reactant (A) comprises alkyl acrylate esters containing at least 8 carbon atoms in the alkyl group.
- 5. The process of claim 1 wherein from about 80 to about 99% by weight of alkyl acrylate monomer (A) is reacted with from about 1 to about 20% by weight of nitrogen containing monomer (B).
- 6. The process of claim 1 wherein monomer (A) comprises a mixture of alkyl acrylate ester monomers.
- 7. The process of claim 1 wherein the alkyl acrylate ester monomers are alkyl methacrylate ester monomers.
- 8. The process of claim 6 wherein the mixture of alkyl acrylate monomers comprises from about 5% to about 75% by weight of alkyl acrylate ester monomers containing from 1 to 11 carbon atoms in the ester alkyl group and from about 25% to about 95% by weight of alkyl acrylate ester monomers containing from 12 to about 24 carbon atoms in the ester alkyl group.
- 9. The process of claim 8 wherein the mixture of alkyl acrylate monomers is reacted with from about 0.1% to about 20% by weight of (B) the at least one nitrogen containing monomer provided that the total equals 100%.
- 10. The process of claim 9 wherein the mixture of alkyl acrylate monomers comprises from about 30% to about 60% by weight of alkyl acrylate ester monomers containing from 1 to 11 carbon atoms in the ester alkyl group and from about 40% to about 70% by weight of alkyl acrylate ester monomers containing from 12 to about 24 carbon atoms in the ester alkyl group, is reacted with from about 0.5% to about 10% by weight of monomer (B).
- 11. The process of claim 1 wherein monomer (A) comprises at least about 5% by weight of alkyl acrylate esters having from 4 to 11 carbon atoms in the ester alkyl group.
- 12. The process of claim 1 wherein monomer (A) comprises from about 5% to about 40% by weight of alkyl acrylate esters having from 1 to 4 carbon atoms in the ester alkyl group.
- 13. The process of claim 1 wherein monomer (A) comprises from about 60% to about 90% by weight of alkyl acrylate esters having from 9 to 11 carbon atoms in the ester alkyl group.
- 14. The copolymer of claim 1 wherein (A) the nitrogen containing monomer is an N-vinyl substituted heterocyclic monomer.
- 15. The process of claim 14 wherein the N-vinyl substituted heterocyclic monomer is at least one member of the group consisting of N-vinyl imidazole, N-vinyl pyrrolidinone and N-vinyl caprolactam.
- 16. The process of claim 1 wherein the vinyl substituted heterocyclic monomer is a vinyl pyridine.
- 17. The process of claim 1 wherein (B) the nitrogen containing monomer is a N,N-dialkylaminoalkyl methacrylamide or methacrylate wherein each alkyl or aminoalkyl group contains, independently, from 1 to about 8 carbon atoms.
- 18. The process of claim 1 wherein (B) the nitrogen containing monomer is tertiary butyl acrylamide.
- 19. The process of claim 1 conducted in a diluent.
- 20. The process of claim 19 wherein the diluent displays Brookfield viscosities measured by procedure ASTM D-2983 ranging from about 50 to about 400 centipoise at −26° C. and from about 100 to about 1500 centipoise at −40° C.
- 21. The process of claim 19 wherein the diluent is a mineral oil.
- 22. The process of claim 21 wherein the mineral oil consists essentially of hydrotreated naphthenic oil.
- 23. The process of claim 21 wherein the mineral oil comprises a hydrodewaxed oil.
- 24. The process of claim 19 wherein the diluent is a synthetic oil.
- 25. The process of claim 24 wherein the synthetic oil is selected from the group consisting of an ester, a polyalphaolefin oligomer or an alkylated benzene.
- 26. The process of claim 19 comprising from about 25% to about 90% by weight of monomers and from about 10% to about 75% by weight of diluent.
- 27. The copolymer prepared by the process of claim 1.
- 28. The copolymer prepared by the process of claim 2.
- 29. The copolymer prepared by the process of claim 19.
- 30. The copolymer of claim 27 having a weight average molecular weight ranging from about 10,000 to about 500,000.
- 31. The copolymer of claim 30 wherein the weight average molecular weight ranges from about 30,000 to about 250,000.
- 32. The copolymer of claim 27 having polydispersity values ranging from about 1.2 to about5.
- 33. The process of claim 1 conducted in an extruder.
- 34. The process of claim 33 wherein the reaction is conducted in the absence of any diluent.
- 35. A lubricating oil composition comprising a major amount of an oil of lubricating viscosity and a minor amount of the copolymer of claim 27.
- 36. A lubricating oil composition comprising a major amount of an oil of lubricating viscosity and a minor amount of the copolymer of claim 28.
- 37. A lubricating oil composition comprising a major amount of an oil of lubricating viscosity and a minor amount of the copolymer of claim 29.
- 38. The lubricating oil composition of claim 35 wherein the oil of lubricating viscosity comprises a mixture of mineral oil and synthetic oils.
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] This application is a continuation-in-part of copending application Ser. No. 08/665,655, filed Jun. 18, 1996, which in turn is a continuation-in-part of copending application Ser. No. 08/492,276, filed Jun. 19, 1995, the disclosures of each being incorporated herein by reference.
Divisions (2)
|
Number |
Date |
Country |
Parent |
09116367 |
Jul 1998 |
US |
Child |
10000515 |
Oct 2001 |
US |
Parent |
08810847 |
Mar 1997 |
US |
Child |
09116367 |
Jul 1998 |
US |
Continuation in Parts (2)
|
Number |
Date |
Country |
Parent |
08665655 |
Jun 1996 |
US |
Child |
08810847 |
Mar 1997 |
US |
Parent |
08492276 |
Jun 1995 |
US |
Child |
08665655 |
Jun 1996 |
US |