Recirculation loop reactor bulk polymerization process
View Patent ↗A process for producing polymer and more particularly adhesive using a recirculating loop reactor. In one embodiment the reactor includes one or more mixers to mix feed stock with the polymerized material recirculating in the reactor. In another embodiment a planetary roller extruder (PRE) may be used for this purpose. In still another embodiment, a combination of one or more static mixers and one or more PREs may be used.
1. A process including the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a recirculating loop reactor having partially polymerized material recirculating therein to form a reaction mixture;
b) heating the reaction mixture to at least the activation temperature of the initiator to produce a polymerized intermediate;
c) recirculating a portion of the polymerized intermediate through the loop reactor while directing a remaining portion of the polymerized intermediate into a removal stream;
d) cooling the recirculating portion of the intermediate to a temperature below the activation temperature of the initiator;
e) mixing the cooled recirculating portion of the intermediate with the feed stock; and
f) subjecting the remaining portion of the polymerized intermediate to further reaction to form polymerized product;
wherein the process converts at least 50% of the monomer to polymerized product.
2. The process of claim 1 wherein the polymerized product is a self-adhesive composition which comprises the polymerization reaction product of at least one alkyl acrylate monomer.
3. The process of claim 1 wherein the reaction loop includes a plurality of static mixers at least one of those static mixers having heat exchange capabilities.
4. The process of claim 1 wherein the residence time of the monomer in the loop reactor is about 1 to about 5 recirculations per hour.
5. The process of claim 1 wherein amount of the recirculating portion and the remaining portion of the polymerized intermediate is regulated by a gear pump in the removal stream.
6. A process including the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a recirculating loop reactor having partially polymerized material recirculating therein to form a reaction mixture;
b) heating the reaction mixture to at least the activation temperature of the initiator to produce a polymerized intermediate;
c) recirculating a portion of the polymerized intermediate through the loop reactor while directing a remaining portion of the polymerized intermediate into a removal stream;
d) cooling the recirculating portion of the intermediate to a temperature below the activation temperature of the initiator;
e) mixing the cooled recirculating portion of the intermediate with the feed stock; and
f) subjecting the remaining portion of the polymerized intermediate to further reaction to form polymerized product;
wherein the reaction mixture contains less than about 5% solvent.
7. The process of claim 6 wherein the pressure in the recirculating loop reactor is greater than about 200 psi.
8. The process of claim 7 wherein the pressure in the loop reactor is about 3,500 psi and up to about 10,000 psi.
9. The process of claim 8 wherein the polymerized intermediate circulates in the recirculating loop reactor as a plug flow.
10. The process of claim 6 wherein the polymerized product has a molecular weight of about 1,500 to 1,000,000.
11. The process of claim 10 wherein the polymerized product has a molecular weight of about 200,000 to about 400,000.
12. The process of claim 1 wherein the process converts at least 95% of the monomer to polymerized product.
13. The process of claim 3 wherein the monomer is resident in the recirculating loop reactor about 15 to 600 minutes.
14. A process comprising the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a planetary roller extruder located in a recirculating loop reactor having a partially polymerized material circulating therein to form a reaction mixture;
b) heating the reaction mixture from step a) to at least the activation temperature of the initiator to polymerize at least one monomer in the feed stock with the partially polymerized material to form a partially polymerized intermediate;
c) recirculating a portion of the partially polymerized intermediate from step b) through a loop reactor while;
d) directing a remaining portion of the partially polymerized intermediate into a stream for removal from the loop reactor;
e) cooling the recirculating portion of the partially polymerized intermediate from step (c) below the activation temperature of the initiator;
f) mixing a portion of the partially polymerized intermediate from step c) with additional feed stock to further polymerize the monomer and the partially polymerized intermediate; and
g) subjecting the remaining portion of the polymerized intermediate to additional reaction to form a polymerized product;
wherein the monomer is resident in the recirculating loop reactor about 15 to 600 minutes.
15. The process of claim 14 wherein the polymerized product is a self-adhesive composition which comprises the polymerization reaction product of at least one alkyl acrylate monomer.
16. The process of claim 14 wherein said planetary roller extruder comprises a plurality of compounding sections including a main spindle surrounded by and intermeshed with a plurality of planetary spindles.
17. The process of claim 14 wherein the amount of the recirculating portion and the removed portion is regulated by a gear pump connected in the removal stream.
18. A process comprising the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a planetary roller extruder located in a recirculating loop reactor having a partially polymerized material circulating therein to form a reaction mixture;
b) heating the reaction mixture from step a) to at least the activation temperature of the initiator to polymerize at least one monomer in the feed stock with the partially polymerized material to form a partially polymerized intermediate;
c) recirculating a portion of the partially polymerized intermediate from step b) through a loop reactor while;
d) directing a remaining portion of the partially polymerized intermediate into a stream for removal from the loop reactor;
e) cooling the recirculating portion of the partially polymerized intermediate from step (c) below the activation temperature of the initiator;
f) mixing a portion of the partially polymerized intermediate from step c) with additional feed stock to further polymerize the monomer and the partially polymerized intermediate; and
g) subjecting the remaining portion of the polymerized intermediate to additional reaction to form a polymerized product;
wherein the reaction mixture contains less than about 5% solvent.
19. The process of claim 18 wherein the pressure in the recirculating loop reactor is greater than about 200 psi.
20. The process of claim 19 wherein the pressure in the loop reactor is about 3,500 psi and up to about 10,000 psi.
21. The process of claim 20 wherein the polymerized intermediate circulates in the recirculating loop reactor as a plug flow.
22. A process comprising the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a planetary roller extruder located in a recirculating loop reactor having a partially polymerized material circulating therein to form a reaction mixture;
b) heating the reaction mixture from step a) to at least the activation temperature of the initiator to polymerize at least one monomer in the feed stock with the partially polymerized material to form a partially polymerized intermediate;
c) recirculating a portion of the partially polymerized intermediate from step b) through a loop reactor while;
d) directing a remaining portion of the partially polymerized intermediate into a stream for removal from the loop reactor;
e) cooling the recirculating portion of the partially polymerized intermediate from step (c) below the activation temperature of the initiator;
f) mixing a portion of the partially polymerized intermediate from step c) with additional feed stock to further polymerize the monomer and the partially polymerized intermediate; and
g) subjecting the remaining portion of the polymerized intermediate to additional reaction to form a polymerized product;
wherein the polymerized product has a molecular weight of about 1,500 to 1,000,000.
23. The process of claim 22 wherein the polymerized product has a molecular weight of about 200,000 to about 400,000.
24. A process comprising the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a planetary roller extruder located in a recirculating loop reactor having a partially polymerized material circulating therein to form a reaction mixture;
b) heating the reaction mixture from step a) to at least the activation temperature of the initiator to polymerize at least one monomer in the feed stock with the partially polymerized material to form a partially polymerized intermediate;
c) recirculating a portion of the partially polymerized intermediate from step b) through a loop reactor while;
d) directing a remaining portion of the partially polymerized intermediate into a stream for removal from the loop reactor;
e) cooling the recirculating portion of the partially polymerized intermediate from step (c) below the activation temperature of the initiator;
f) mixing a portion of the partially polymerized intermediate from step c) with additional feed stock to further polymerize the monomer and the partially polymerized intermediate; and
g) subjecting the remaining portion of the polymerized intermediate to additional reaction to form a polymerized product;
wherein the process converts at least 50% of the monomer to polymerized product.
25. The process of claim 24 wherein the process converts at least 95% of the monomer to polymerized product.
26. A recirculation loop reactor process including the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a loop reactor having a partially polymerized material recirculating therethrough to form a polymerizable mixture;
b) heating the mixture from step a) to at least the activation temperature of the initiator in the reaction to polymerize the monomer and the partially polymerized material and form a polymerized intermediate;
c) circulating a portion of the polymerized intermediate from step b) through a loop reactor while cooling it to a temperature below the activation temperature of the initiator at a predetermined flow;
d) mixing the cooled circulating material from step c) with additional feed stock to further polymerize the monomer and the polymerized intermediate;
e) directing a remaining portion of the further polymerized intermediate into a stream for removal from the loop reactor; and
f) subjecting the remaining portion of the polymerized intermediate to an additional reaction in a planetary roller extruder to reduce the unreacted monomer and form a polymerized product;
wherein the monomer is resident in the recirculating loop reactor about 15 to 600 minutes.
27. The process of claim 20 wherein the polymerized product is a self-adhesive composition which comprises the polymerization reaction product of at least one alkyl acrylate monomer.
28. The process of claim 26 wherein said planetary roller extruder comprises a plurality of compounding sections including a main spindle surrounded by and intermeshed with a plurality of planetary spindles.
29. The process of claim 26 wherein the amount of the recirculating portion and the remaining portion is regulated by a gear pump in the removal stream.
30. A recirculation loop reactor process including the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a loop reactor having a partially polymerized material recirculating therethrough to form a polymerizable mixture;
b) heating the mixture from step a) to at least the activation temperature of the initiator in the reaction to polymerize the monomer and the partially polymerized material and form a polymerized intermediate;
c) circulating a portion of the polymerized intermediate from step b) through a loop reactor while cooling it to a temperature below the activation temperature of the initiator at a predetermined flow;
d) mixing the cooled circulating material from step c) with additional feed stock to further polymerize the monomer and the polymerized intermediate;
e) directing a remaining portion of the further polymerized intermediate into a stream for removal from the loop reactor; and
f) subjecting the remaining portion of the polymerized intermediate to an additional reaction in a planetary roller extruder to reduce the unreacted monomer and form a polymerized product;
wherein the reaction mixture contains less than about 5% solvent.
31. The process of claim 30 wherein the pressure in the recirculating loop reactor is greater than about 200 psi.
32. The process of claim 31 wherein the pressure in the loop reactor is about 3,500 psi and up to about 10,000 psi.
33. The process of claim 32 wherein the polymerized intermediate circulates in the recirculating loop reactor as a plug flow.
34. A recirculation loop reactor process including the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a loop reactor having a partially polymerized material recirculating therethrough to form a polymerizable mixture;
b) heating the mixture from step a) to at least the activation temperature of the initiator in the reaction to polymerize the monomer and the partially polymerized material and form a polymerized intermediate;
c) circulating a portion of the polymerized intermediate from step b) through a loop reactor while cooling it to a temperature below the activation temperature of the initiator at a predetermined flow;
d) mixing the cooled circulating material from step c) with additional feed stock to further polymerize the monomer and the polymerized intermediate;
e) directing a remaining portion of the further polymerized intermediate into a stream for removal from the loop reactor; and
f) subjecting the remaining portion of the polymerized intermediate to an additional reaction in a planetary roller extruder to reduce the unreacted monomer and form a polymerized product;
wherein the polymerized product has a molecular weight of about 1,500 to 1,000,000.
35. The process of claim 34 wherein the polymerized product has a molecular weight of about 200,000 to about 400,000.
36. A recirculation loop reactor process including the steps of:
a) introducing a feed stock containing at least one monomer and at least one activatable initiator into a loop reactor having a partially polymerized material recirculating therethrough to form a polymerizable mixture;
b) heating the mixture from step a) to at least the activation temperature of the initiator in the reaction to polymerize the monomer and the partially polymerized material and form a polymerized intermediate;
c) circulating a portion of the polymerized intermediate from step b) through a loop reactor while cooling it to a temperature below the activation temperature of the initiator at a predetermined flow;
d) mixing the cooled circulating material from step c) with additional feed stock to further polymerize the monomer and the polymerized intermediate;
e) directing a remaining portion of the further polymerized intermediate into a stream for removal from the loop reactor; and
f) subjecting the remaining portion of the polymerized intermediate to an additional reaction in a planetary roller extruder to reduce the unreacted monomer and form a polymerized product;
wherein the process converts at least 50% of the monomer to polymerized product.
37. The process of claim 36 wherein the process converts at least 95% of the monomer to polymerized product.