Continuous bulk polymerization of vinyl monomers
View Patent ↗A method for continuous bulk polymerization is disclosed that includes providing a planetary roller extruder having a plurality of planetary roller zones, introducing an acrylate monomer, a di-vinyl monomer, and a hydroxyl functional acrylic monomer into the planetary roller extruder, introducing an initiator into the planetary roller extruder for initiation of a free-radical polymerization of the acrylate monomer, the di-vinyl monomer, and the hydroxyl functional acrylic monomer to form an acrylic polymer, maintaining the temperature of the free-radical polymerization in the planetary roller extruder below 240° C., and discharging a portion of the acrylic polymer from the planetary roller extruder, and returning the portion of the acrylic polymer to one or more of the plurality of planetary roller zones.
1. A method for continuous bulk polymerization of an acrylic pressure-sensitive adhesive, the method comprising:
providing a planetary roller extruder having a plurality of planetary roller zones;
introducing an alkyl acrylate monomer and one or more other vinylic monomers into the planetary roller extruder;
introducing an initiator into the planetary roller extruder for initiation of a free-radical polymerization of the alkyl acrylate monomer and the one or more other vinylic monomers to form an acrylic polymer;
maintaining the temperature of the free-radical polymerization in the planetary roller extruder below 240° C.; and
discharging a portion of the acrylic polymer from the planetary roller extruder, and returning the portion of the acrylic polymer to one or more of the plurality of planetary roller zones.
2. The method of claim 1 wherein the acrylic polymer comprises, by weight, about 65% to about 95% alkyl acrylate monomer.
3. The method of claim 2 wherein the acrylic polymer comprises, by weight, about 5% to about 25% vinyl acetate as one of the one or more other vinylic monomers.
4. The method of claim 2 wherein the acrylic polymer comprises, by weight, up to about 11% di-vinyl monomer.
5. The method of claim 3 wherein the acrylic polymer comprises, by weight, about 1% to about 9% acrylic acid.
6. The method of claim 2 wherein the alkyl acrylate monomer comprises an alkyl group with from 2 to 20 carbon atoms.
7. The method of claim 2 wherein the alkyl acrylate monomer is selected from the group consisting of 2-ethylhexyl acrylate, butyl acrylate, isooctyl acrylate, isodecyl acrylate, and combinations thereof.
8. The method of claim 2 wherein the other vinylic monomers are selected from the group consisting of styrene, alpha methyl styrene, tetraethylene glycol diacrylate, hydroxyethyl methacrylate, vinyl acetate, and combinations thereof.
9. The method of claim 1 wherein the acrylic polymer is a random copolymer.
10. The method of claim 1 further comprising introducing a solvent into one or more of the plurality of planetary roller zones.
11. A method for continuous bulk polymerization of an acrylic pressure-sensitive adhesive, the method comprising:
providing a planetary roller extruder having a plurality of planetary roller zones;
introducing an acrylate monomer and an initiator into the planetary roller extruder as an initial introduction of materials;
heating the initial introduction of materials to initiate a free-radical polymerization thereof to form an acrylic polymer;
introducing into the planetary roller extruder, downstream of the initial introduction of materials, a mixture of additional acrylate monomer and initiator;
maintaining the temperature of the free-radical polymerization in the planetary roller extruder below 240° C.; and
discharging a portion of the acrylic polymer from a transfer pipe of the planetary roller extruder, and introducing the portion of the acrylic polymer to one or more of the plurality of planetary roller zones.
12. The method of claim 11 wherein introducing the initial introduction of materials further comprises introducing a di-vinyl monomer into the planetary roller extruder.
13. The method of claim 11 wherein introducing the initial introduction of materials further comprises introducing acrylic acid and/or hydroxyethyl methacrylate into the planetary roller extruder.
14. The method of claim 11 wherein the acrylic polymer comprises, by weight, about 65% to about 95% of an alkyl acrylate monomer.
15. The method of claim 13 wherein the acrylic polymer comprises, by weight, about 5% to about 25% vinyl acetate.
16. The method of claim 15 wherein the acrylic polymer comprises, by weight, about 1% to about 9% acrylic acid.
17. The method of claim 11 wherein the acrylate monomer comprises one or more alkyl acrylate monomers having an alkyl group with from 2 to 20 carbon atoms.
18. The method of claim 14 wherein the alkyl acrylate monomer is selected from the group consisting of 2-ethylhexyl acrylate, butyl acrylate, isooctyl acrylate, isodecyl acrylate, and combinations thereof.
19. The method of claim 12 wherein the acrylate monomers are selected from the group consisting of tetraethylene glycol diacrylate, hydroxyethyl methacrylate, methyl methacrylate, ethylacrylate, methylacrylate, propylacrylate, propylmethacrylate, hexylacrylate, hexylmethacrylate, and combinations thereof.
20. The method of claim 11 further comprising introducing a solvent into one or more of the plurality of planetary roller zones.
21. The method of claim 11 wherein introducing the initial introduction of materials further comprises introducing other vinylic monomers into the planetary roller extruder.
22. The method of claim 21 wherein the other vinylic monomers comprise styrene, alpha methyl styrene, and vinyl acetate, and combinations thereof.