Furanoate-based polyester and copolyester compositions using falling strand devolatilization

Patent metadata

Field	Value
Publication number	US-11072690-B2
Application number	US-201615780906-A
Country	US
Kind code	B2
Filing date	Dec 2, 2016
Priority date	Dec 3, 2015
Publication date	Jul 27, 2021
Grant date	Jul 27, 2021

Abstract

Polymers and copolymers, and systems and methods for processing the same. Advantageously, the polymers and copolymers of the present invention have undergone processing in a falling strand devolatilizer and rotary disk finisher such that a low-cost, low-energy, and high-production-rate product is produced.

First claim

What is claimed is:

1. A process for melt-state polymerization of polyesters or co-polyesters, comprising:
a) melting polyester or co-polyester pellets, wherein the polyester or co-polyester pellets comprise a furanoate-based polyester or copolyester, to form a feed resin;
b) flowing the feed resin vertically downward in the form of strands, thin films, filaments, or ribbons to increase the surface area and provide a devolatilized resin; and
c) pelletizing the devolatilized resin.

2. A process according to claim 1 , wherein step b) of flowing the feed resin vertically downward in the form of thin films, filaments, or ribbons occurs by extruding the feed resin into an evacuated chamber.

3. A process according to claim 1 , wherein step b) of flowing the feed resin vertically downward in the form of thin films, filaments, or ribbons occurs by extruding the feed resin into a falling strand devolatilizer/finisher.

4. A process according to claim 3 , further comprising the step of increasing the intrinsic viscosity (IV) of the devolatilized resin in a rotary disk-type finisher after extruding the feed resin into a falling strand devolatilizer/finisher.

5. A process according to claim 1 , wherein step a) of melting polyester or co-polyester pellets to form a feed resin further comprises compounding an inorganic additive and/or an organic additive with the polyester or co-polyester pellets to form the feed resin.

6. A process according to claim 1 , wherein the intrinsic viscosity (IV) of the devolatilized resin is greater than the intrinsic viscosity (IV) of the feed resin.

7. A process according to claim 1 , further comprising the step of extruding the devolatilized resin into a second falling strand devolatilizer/finisher after step b), wherein the polyester or co-polyester pellets comprise poly(ethylene-2,5-furandicarboxylate) (PEF); poly(trimethylene-2,5-furandicarboxylate) (PTF); or poly(butylene-2,5-furandicarboxylate) (PBF).

8. A process according to claim 1 , further comprising the step(s) of:
i) processing the devolatilized resin in a rotary disk-type finisher after step b); or
ii) extruding the devolatilized resin into a second falling strand devolatilizer/finisher after step b); or
iii) both steps i) and ii) in any sequence.

9. The process according to claim 1 , wherein step c) of pelletizing the devolatilized resin further comprises compounding the devolatilized resin with at least one inorganic additive and/or at least one organic additive.

10. A process according to claim 1 , wherein the devolatilized polyester or co-polyester resin is compounded to an intrinsic viscosity of from about 0.50 dL/g to about 0.95 dL/g.

11. A process according to claim 1 , wherein the intrinsic viscosity of the devolatilized polyester or co-polyester resin exceeds the intrinsic viscosity of a devolatilized polyester or co-polyester resin processed by a conventional SSP process by at least 25%, under otherwise similar conditions.

12. A process according to claim 1 , wherein the devolatilized resin yellowness b*, as measured by Cielab b*, is lower than the feed resin yellowness b*.

13. A process according to claim 1 , wherein the polyester or co-polyester pellets comprise poly(ethylene-2,5-furandicarboxylate) (PEF); poly(trimethylene-2,5-furandicarboxylate) (PTF); poly(butylene-2,5-furandicarboxylate) (PBF); poly(isosorbide-2,5-furandicarboxylate) (PISF); poly(isoidide-2,5-furandicarboxylate) (PIIF); poly(isomannide-2,5-furandicarboxylate) (PIMF); poly(neopentyl-2,5-furandicarboxylate) (PNPGF); poly(ethylene-2,5-furandicarboxylate) with 10 mol. % 1,8-naphthalene dicarboxylate (PEF-PEN), poly(1,4-phenylene-2,5-furandicarboxylate) (PCHF); poly(1,2-dimethylphenylene-2,5-furandicarboxylate) (PDMFF); or any combinations thereof.

14. A process according to claim 1 , wherein the polyester or co-polyester further comprises an electron-deficient alkene selected from dimethyl maleate, maleic acid, an acrylate, acrylic acid, or a halogenated alkyl-substituted alkene.

15. A process according to claim 1 , wherein the polyester or co-polyester further comprises at least one chain architecture modifying agent selected from a multimaleamide, a multiacrylate, a bisnitroalkene, an amide-substituted alkene, an imide-substituted alkene, a haloalkyl-substituted alkene, a multioxazoline, a multiepoxide, a multilactone, an exocyclic reactive compound, or a combination thereof.

16. A process according to claim 1 , wherein the polyester or co-polyester further comprises a chain architecture modifying agent in a concentration of from about 0.0001% to about 20%.

17. A process for melt-state polymerization of polyesters and co-polyesters, comprising:
a) melting a furanoate-based polyester or co-polyester pellets to form a resin melt;
b) flowing the resin melt vertically downward in one or more strands, thin films, filaments, or ribbons in a first vacuum reactor to increase surface area and provide a devolatilized resin melt;
c) increasing the intrinsic viscosity of the devolatilized resin melt in a rotary disk-type finisher;
d) flowing the devolatilized resin melt from step c) vertically downward in one or more strands, thin films, filaments, or ribbons in a second vacuum reactor to increase surface area and provide a further devolatilized resin; and
e) pelletizing the further devolatilized resin.

18. A process according to claim 17 , wherein the polyester or co-polyester pellets comprise poly(ethylene-2,5-furandicarboxylate) (PEF); poly(trimethylene-2,5-furandicarboxylate) (PTF); poly(butylene-2,5-furandicarboxylate) (PBF); poly(isosorbide-2,5-furandicarboxylate) (PIS F); poly(isoidide-2,5-furandicarboxylate) (PIIF); poly(isomannide-2,5-furandicarboxylate) (PIMF); poly(neopentyl-2,5-furandicarboxylate) (PNPGF); poly(ethylene-2,5-furandicarboxylate) with 10 mol. % 1,8-naphthalene dicarboxylate (PEF-PEN), poly(1,4-phenylene-2,5-furandicarboxylate) (PCHF); poly(1,2-dimethylphenylene-2,5-furandicarboxylate) (PDMFF); or any combinations thereof.

19. A process for melt-state polymerization of polyesters and co-polyesters, comprising:
a) melting a furanoate-based polyester or co-polyester pellets to form a resin melt;
b) flowing the resin melt vertically downward in one or more strands, thin films, filaments, or ribbons by extruding the feed resin into a falling strand devolatilizer/finisher to provide a devolatilized resin melt;
c) optionally, increasing the intrinsic viscosity of the devolatilized resin melt in a rotary disk-type finisher; and
d) compounding the devolatilized resin with at least one inorganic additive and/or at least one organic additive and pelletizing the devolatilized resin;
wherein the furanoate-based polyester or co-polyester further comprises at least one chain architecture modifying agent.

Assignees

• Coca Cola Co

Inventors

• Moffitt Ronald D
• Kaur Jasmeet

Classifications

• B29C49/071

  Preforms or parisons characterised by their configuration, e.g. geometry, dimensions or physical properties · CPC title

• B29C2949/0715

  the preform having one end closed · CPC title

• C08J2367/00

  Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers · CPC title

• B29B2013/005

  Degassing undesirable residual components, e.g. gases, unreacted monomers, from material to be moulded · CPC title

• B29C48/287

  Raw material pre-treatment while feeding (B29C48/78 takes precedence) · CPC title