Polymer compositions and methods
US-9453100-B2 · Sep 27, 2016 · US
US11230625B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11230625-B2 |
| Application number | US-201916387788-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 18, 2019 |
| Priority date | Apr 18, 2018 |
| Publication date | Jan 25, 2022 |
| Grant date | Jan 25, 2022 |
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Described herein are methods of preparing poly(alkylene carbonate) polymers comprising an increased ratio of primary hydroxyl end groups to secondary hydroxyl end groups, and compositions thereof.
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The invention claimed is: 1. A method for increasing the ratio of primary to secondary OH end groups of a poly(propylene carbonate) (“PPC”) polymer composition, the method comprising steps of copolymerizing propylene oxide and CO 2 in the presence of a copolymerization catalyst to form a reaction mixture comprising unquenched copolymerization catalyst and a starting PPC polymer composition, heating the reaction mixture comprising unquenched copolymerization catalyst and the starting PPC polymer composition to provide a reaction mixture comprising the unquenched copolymerization catalyst and a modified PPC polymer composition, wherein the modified PPC polymer composition has a higher ratio of primary to secondary OH end groups relative to the starting PPC polymer composition; and contacting the reaction mixture comprising unquenched copolymerization catalyst and the modified PPC polymer composition with a quenching agent suitable to end the copolymerization reaction. 2. The method of claim 1 , comprising heating the reaction mixture comprising unquenched copolymerization catalyst and starting PPC polymer composition to a temperature in the range of about 50° C. to about 85° C. 3. The method of claim 1 , wherein the starting PPC polymer composition has an Mn of about 500 to about 30,000 g/mol. 4. The method of claim 1 , wherein the molar percent of primary OH end groups in the modified PPC polymer composition is at least 15%, at least 20%, at least 25%, at least 30%, at least 35%, at least 40%, at least 45%, at least 50%, at least 51%, at least 70%, at least 75%, at least 80%, at least 85%, at least 90%, or at least 95% greater than the molar percent of primary OH end groups in the starting PPC polymer. 5. The method of claim 1 , wherein the ratio of primary OH end groups to secondary OH end groups in the modified PPC polymer composition is at least 75%, at least 100%, at least 150%, at least 200%, at least 300%, at least 400%, or at least 500% greater than the ratio of primary OH end groups to secondary OH end groups in the starting PPC polymer composition. 6. The method of claim 1 , comprising venting the CO 2 from the reaction mixture prior to the heating step. 7. The method of claim 1 , wherein the quenching agent is added to the reaction mixture after the ratio of primary to secondary OH end groups has increased to a desired level and/or by a desired amount. 8. The method of claim 1 , wherein an amount of cyclic propylene carbonate (“cPC”) formed during the heating step is less than about 10 weight percent, about 9 weight percent, about 8 weight percent, about 7 weight percent, about 6 weight percent, about 5 weight percent, about 4 weight percent, about 3 weight percent, about 2 weight percent, or about 1 weight percent relative to the starting PPC polymer. 9. The method of claim 1 , wherein the heating step is performed in a continuous flow format. 10. The method of claim 9 , further comprising drawing the starting PPC composition from a feed reservoir, flowing the PPC through a heated zone and accumulating the modified PPC composition in a product reservoir. 11. The method of claim 8 , further comprising the step of removing cPC. 12. The method of claim 11 , wherein the cPC is removed continuously during the heating step. 13. The method of claim 12 , wherein the removal of the cPC during the heating step is facilitated by reduced pressure. 14. The method of claim 12 , wherein the removal of the cPC during the heating step is facilitated by a gas flow. 15. The method of claim 4 , wherein the molar percent of primary OH end groups in the modified PPC polymer composition is about 35% greater than the molar percent of primary OH end groups in the starting PPC polymer. 16. The method of claim 4 , wherein the molar percent of primary OH end groups in the modified PPC polymer composition is at least 45% greater than the molar percent of primary OH end groups in the starting PPC polymer. 17. The method of claim 4 , wherein the molar percent of primary OH end groups in the modified PPC polymer composition is at least 70%, at least 75%, at least 80%, at least 85%, at least 90%, or at least 95% greater than the molar percent of primary OH end groups in the starting PPC polymer. 18. The method of claim 4 , wherein the molar percent of primary OH end groups in the starting PPC polymer composition is less than 15%, less than 10%, less than 8%, less than 5%, or less than 3%, or less than 2%. 19. The method of claim 1 , wherein the molar percent of primary and secondary OH end groups is determined by 1 H NMR. 20. The method of claim 8 , wherein the molar percent of the cPC is determined by NMR. 21. The method of claim 1 , comprising heating the reaction mixture comprising unquenched copolymerization catalyst and starting PPC polymer composition to a temperature in the range of about 50° C. to about 70° C. 22. The method of claim 1 , comprising heating the reaction mixture comprising unquenched copolymerization catalyst and starting PPC polymer composition to a temperature of about 65° C.
saturated · CPC title
Post-polymerisation treatment · CPC title
and cyclic ethers · CPC title
Materials · CPC title
containing carboxylic acids or their salts {(B01J31/0277 - B01J31/0298 take precedence; multi-metal carboxylate complexes like Pd (II) acetate, i.e. Pd3 (OAc) 6 or Cr(II)acetate, i.e. Cr2(OAc)4 B01J31/2226)} · CPC title
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