Articles comprising copolyesters produced with germanium catalyst
US-2024376258-A1 · Nov 14, 2024 · US
US9346915B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9346915-B2 |
| Application number | US-201314372621-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 25, 2013 |
| Priority date | Feb 14, 2012 |
| Publication date | May 24, 2016 |
| Grant date | May 24, 2016 |
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A method for producing a polymer, including: (i) continuously supplying and bringing at least a first monomer, which is ring-opening polymerizable, and a compressive fluid into contact with each other, to thereby allow the first monomer to carry out ring-opening polymerization to continuously generate an intermediate; and (ii) bringing the intermediate and a second monomer, which is identical to or different from the first monomer in kind, into contact with each other, to thereby allow the intermediate and the second monomer to carry out polymerization.
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The invention claimed is: 1. A method for producing a polymer, comprising: (i) continuously supplying and bringing a first monomer, which is ring-opening polymerizable, a catalyst, and a first compressive fluid into contact with each other, to thereby allow the first monomer to carry out ring-opening polymerization and to continuously generate a composition comprising an intermediate; and (ii) continuously supplying and bringing a second monomer, which is identical to the first monomer, and a second compressive fluid which is identical to the first compressive fluid into contact with the composition comprising the intermediate, to thereby allow the intermediate and the second monomer to carry out polymerization and produce said polymer. 2. The method for producing a polymer according to claim 1 , wherein in (i) the first monomer and the compressive fluid are continuously supplied under the following conditions, to thereby bring the first monomer and the first compressive fluid into contact with each other: Feeding speed of the first monomer ( g / min ) Feeding speed of the first compressive fluid ( g / min ) ≥ 1. 3. The method for producing a polymer according to claim 1 , wherein the continuously supplying and bringing the first monomer and the first compressive fluid into contact with each other makes the first monomer melt. 4. The method for producing a polymer according to claim 1 , wherein the catalyst is an organic catalyst free from a metal atom. 5. The method for producing a polymer according to claim 1 , wherein a lower limit of a temperature during the ring-opening polymerization in (i) is 40° C., and an upper limit of the temperature during the ring-opening polymerization in (i) is 150° C., or a temperature that is higher than a melting point of the first monomer by 50° C., whichever higher. 6. The method for producing a polymer according to claim 1 , wherein a monomer conversion amount of each of the first monomer and the second monomer is 98 mol % or higher. 7. The method for producing a polymer according to claim 1 , wherein the polymer has a number average molecular weight of 12,000 or greater. 8. The method for producing a polymer according to claim 1 , wherein the compressive fluid comprises carbon dioxide. 9. The method for producing a polymer according to claim 4 , wherein the organic catalyst free from a metal atom is a basic nucleophilic nitrogen compound. 10. The method for producing a polymer according to claim 1 , wherein the first monomer is a monomer having a ring structure containing an ester bond therein. 11. The method for producing a polymer according to claim 1 , wherein the compressive fluid is carbon dioxide and the first and second monomer is L-lactide, D-lactide, or a mixture thereof, and wherein the polymer produced has a number average molecular weight of 12,000-200,000. 12. The method for producing a polymer according to claim 1 , wherein the polymer produced is substantially free from an organic solvent, and comprises less than 2 mol % of said monomers. 13. The method for producing a polymer according to claim 1 , wherein the polymer produced is substantially free from an organic solvent, and comprises 1,000 ppm or less of said monomers. 14. The method for producing a polymer according to claim 11 , wherein the polymer produced is substantially free from an organic solvent, and comprises less than 2 mol % of said monomers. 15. The method for producing a polymer according to claim 11 , wherein the polymer produced is substantially free from an organic solvent, and comprises 1,000 ppm or less of said monomers.
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