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| 국가/구분 | United States(US) Patent 등록 |
|---|---|
| 국제특허분류(IPC7판) |
|
| 출원번호 | US-0264602 (2008-11-04) |
| 등록번호 | US-8765217 (2014-07-01) |
| 발명자 / 주소 |
|
| 출원인 / 주소 |
|
| 대리인 / 주소 |
|
| 인용정보 | 피인용 횟수 : 1 인용 특허 : 318 |
A method of preparing a (meth)acrylate syrup comprises: providing one or more precursors for formation of (meth)acrylate monomer; continuously forming the (meth)acrylate monomer from the one or more precursors thereof; and continuously polymerizing at least the (meth)acrylate monomer to form the (me
A method of preparing a (meth)acrylate syrup comprises: providing one or more precursors for formation of (meth)acrylate monomer; continuously forming the (meth)acrylate monomer from the one or more precursors thereof; and continuously polymerizing at least the (meth)acrylate monomer to form the (meth)acrylate syrup. The (meth)acrylate syrup is useful in, for example, preparation of adhesives.
1. A method of preparing a (meth)acrylate syrup comprising: providing one or more precursors for formation of (meth)acrylate monomer;continuously forming the (meth)acrylate monomer from the one or more precursors thereof;continuously polymerizing at least the (meth)acrylate monomer to form the (meth
1. A method of preparing a (meth)acrylate syrup comprising: providing one or more precursors for formation of (meth)acrylate monomer;continuously forming the (meth)acrylate monomer from the one or more precursors thereof;continuously polymerizing at least the (meth)acrylate monomer to form the (meth)acrylate syrup; andhalting polymerization once the (meth)acrylate syrup is formed,wherein the method is a continuous process that is essentially uninterrupted in time and space from a beginning reference point preceding formation of the (meth)acrylate monomer to an ending reference point that is no earlier in the process than a point at which the (meth)acrylate syrup is formed therefrom,wherein the (meth)acrylate syrup is formed using a reactor for formation of the (meth)acrylate monomer coupled to a polymerization reactor for continuously receiving the (meth)acrylate monomer from the reactor in which it is formed and partially polymerizing the (meth)acrylate monomer to form the (meth)acrylate syrup by exposing on a portion of the (meth)acrylate monomer at a time to reaction conditions within the polymerization reactor, andwherein continuously polymerizing at least the (meth)acrylate monomer occurs within a tubing network within a heat transfer medium and heat is continuously supplied from the heat transfer medium to the polymerization reactor during steady state operation of the polymerization reactor. 2. The method of claim 1, wherein continuously forming the (meth)acrylate monomer comprises reacting a (meth)acryloyl chloride and its corresponding oxo alcohol. 3. The method of claim 1, wherein continuously forming the (meth)acrylate monomer comprises esterification of (meth)acrylic acid and its corresponding oxo alcohol. 4. The method of claim 3, wherein the oxo alcohol comprises a chain of at least six carbon atoms. 5. The method of claim 3, wherein the esterification occurs at an elevated temperature in the presence of at least one organic sulfonic acid catalyst. 6. The method of claim 1, wherein the (meth)acrylate monomer has an atmospheric boiling temperature of at least about 140° C. 7. The method of claim 1, further comprising optionally purifying the (meth)acrylate monomer after its formation and prior to polymerization thereof. 8. The method of claim 1, wherein continuously polymerizing at least the (meth)acrylate monomer to form the (meth)acrylate syrup comprises polymerizing at least one continuously formed (meth)acrylate monomer and at least one other type of monomer. 9. The method of claim 1, wherein continuous polymerization of at least the (meth)acrylate monomer is halted prior to near complete conversion of the (meth)acrylate monomer. 10. The method of claim 1, wherein continuous polymerization of at least the (meth)acrylate monomer is halted at a point corresponding to about 5% to about 15% conversion of the (meth)acrylate monomer. 11. The method of claim 1, wherein continuously polymerizing at least the (meth)acrylate monomer is an essentially solvent-free process. 12. The method of claim 1, wherein continuous polymerization of at least the (meth)acrylate monomer is capable of efficiently proceeding at temperatures of less than about 150° C. 13. The method of claim 1, wherein continuously polymerizing at least the (meth)acrylate monomer occurs wherein the continuous polymerization reaction temperature is less than atmospheric boiling point of the (meth)acrylate monomer being polymerized to a syrup by at least about 30° C. 14. The method of claim 1, wherein continuously polymerizing at least the (meth)acrylate monomer occurs wherein the continuous polymerization reaction temperature is less than atmospheric boiling point of the (meth)acrylate monomer being polymerized to a syrup by at least about 50° C. 15. The method of claim 1, wherein continuously polymerizing at least the (meth)acrylate monomer comprises using a polymerization initiator having a half life of about ten hours or less at a use temperature of about 70° C. or less. 16. The method of claim 1, wherein continuously polymerizing at least the (meth)acrylate monomer occurs within a heated portion of the polymerization reactor and with a residence time therein of less than about thirty minutes. 17. The method of claim 1, wherein continuously polymerizing at least the (meth)acrylate monomer occurs within a heated portion of the polymerization reactor and with a residence time therein of less than about five minutes. 18. The method of claim 1, wherein continuously polymerizing at least the (meth)acrylate monomer occurs within a heated portion of the polymerization reactor and wherein less than about 10% of continuous volumetric throughput is present within the heated portion of the polymerization reactor at any given time. 19. The method of claim 1, wherein the method is performed in a polymerization system closed to atmospheric air. 20. The method of claim 19, further comprising purging oxygen from the system prior to or while continuously polymerizing at least the (meth)acrylate monomer to form the (meth)acrylate syrup. 21. The method of claim 19, further comprising a step of exposing the (meth)acrylate syrup to atmospheric oxygen to activate any polymerization inhibitors that are present. 22. The method of claim 19, further comprising a step of adding at least one polymerization inhibitor to the (meth)acrylate syrup once the (meth)acrylate syrup is formed. 23. The method of claim 1, wherein the tubing network is a compressed tubing network. 24. The method of claim 1, wherein the (meth)acrylate syrup formed is storage stable. 25. The method of claim 1, wherein the (meth)acrylate syrup has a Brookfield viscosity of about 0.2 Pascal-second to about 10 Pascal-seconds when measured at room temperature. 26. The method of claim 1, wherein the (meth)acrylate syrup has a Brookfield viscosity of about 0.5 Pascal-second to about 5 Pascal-seconds when measured at room temperature. 27. The method of claim 1, wherein the (meth)acrylate syrup has a Brookfield viscosity of about 1 Pascal-second to about 3 Pascal-seconds when measured at room temperature. 28. The method of claim 1, wherein the (meth)acrylate syrup has a range of polydispersity. 29. The method of claim 1, further comprising a step of bringing the (meth)acrylate syrup to approximately room temperature. 30. The method of claim 1, wherein the step of continuously polymerizing at least the (meth)acrylate monomer to form the (meth)acrylate syrup comprises progressively heating the (meth)acrylate monomer. 31. The method of claim 1, wherein the (meth)acrylate syrup is continuously supplied to further processing equipment. 32. A method of preparing an adhesive film, comprising: preparing a (meth)acrylate syrup according to the method of claim 1;continuously coating a composition comprising the (meth)acrylate syrup onto a substrate; andpolymerizing the composition comprising the (meth)acrylate syrup to form the adhesive film. 33. The method of claim 32, wherein polymerizing the composition comprises free radical polymerization.
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