Methods for processing and plasticizing poly(ethylene furanoate) preforms by water sorption

Patent metadata

Field	Value
Publication number	US-10940630-B2
Application number	US-201515511382-A
Country	US
Kind code	B2
Filing date	Sep 15, 2015
Priority date	Sep 16, 2014
Publication date	Mar 9, 2021
Grant date	Mar 9, 2021

Abstract

This disclosure provides effective methods for expanding the processing window for poly(ethylene furanoate) (PEF) and poly(ethylene furanoate) co-polymer (PEF co-polymer) polyester preforms, such that these preforms can be beneficially used in the fabrication of bottles and containers, including bottles for carbonated soft drinks. The processing window is expanded by, for example, pre-conditioning the PEF or PEF co-polymer preform prior to stretch blow-molding by contacting the PEF or PEF co-polymer preform with water or high (>50%) relative humidity air for a desired time period and at a temperature greater than or equal to ambient temperature, to take advantage of the unique and unexpected properties afforded the preform by water sorption at these temperatures.

First claim

We claim:

1. A method of pre-conditioning a poly(ethylene furanoate) or poly(ethylene furanoate) co-polymer preform for stretch blow-molding, the method comprising:
a) providing or having a poly(ethylene furanoate) (PEF) or poly(ethylene furanoate) co-polymer (PEF co-polymer) preform; and
b) contacting the PEF or PEF co-polymer preform with liquid water at a temperature of about 80° C. for up to about 15 h; and
c) drying the PEF or PEF co-polymer preform to a water concentration of less than 40 to 50 ppm of water in the PEF or PEF co-polymer preform.

2. The method of claim 1 , wherein the PEF or PEF co-polymer preform comprises a modifier that offsets the effects of residual water in the PEF or PEF co-polymer preform or reduces solid state polymerization time.

3. The method of claim 2 , wherein the modifier extends chain length of PEF or PEF co-polymer in the PEF or PEF co-polymer preform.

4. The method of claim 2 , wherein the modifier is an anhydride, epoxide, or oxazoline.

5. The method of claim 2 , wherein the modifier increases intrinsic viscosity or molecular weight of PEF or PEF co-polymer in the PEF or PEF co-polymer preform.

6. The method of claim 2 , wherein the modifier constitutes about 0.02 wt % to about 0.9 wt % of the PEF or PEF co-polymer preform.

7. The method of claim 1 , further comprising subjecting the PEF or PEF co-polymer preform to a solid state polymerization (SSP) process so as to increase an average intrinsic viscosity to form a PEF or PEF co-polymer preform having an average intrinsic viscosity (IV) greater than or equal to about 0.8 dl/g.

8. The method of claim 1 , wherein the pre-conditioned PEF or PEF co-polymer preform has a lower glass transition temperature relative to an unconditioned PEF or PEF co-polymer preform.

9. The method of claim 1 , further comprising the following steps after the contacting step and before the drying step:
i) removing the PEF or PEF co-polymer preform from the liquid water;
ii) tumbling the PEF or PEF co-polymer preform to remove trapped water in the PEF or PEF co-polymer preform; and
iii) removing surface water from the PEF or PEF co-polymer preform using an air-knife or a fan.

10. A pre-conditioned poly(ethylene furanoate) (PEF) or poly(ethylene furanoate) co-polymer (PEF co-polymer) preform made according to claim 1 .

11. A method for making a poly(ethylene furanoate) or poly(ethylene furanoate) co-polymer container, the method comprising:
a) pre-conditioning a poly(ethylene furanoate) (PEF) or poly(ethylene furanoate) co-polymer (PEF co-polymer) preform according to claim 1 to form a pre-conditioned PEF or PEF co-polymer preform; and
b) stretch blow-molding the pre-conditioned PEF or PEF co-polymer preform to form a PEF or PEF co-polymer container.

12. The method of claim 11 , wherein the stretch blow-molding step occurs in a process window that is defined from about 5° C. above the glass transition temperature of the pre-conditioned PEF or PEF co-polymer preform to about 5° C. below the crystallization temperature of the pre-conditioned PEF or PEF co-polymer preform.

13. The method of claim 11 , wherein the pre-conditioned PEF or PEF co-polymer preform is stretch blow-molded to form the PEF or PEF co-polymer container at a temperature, a pressure, or both that is/are lower than the corresponding temperature, pressure, or both needed to stretch blow-mold a comparable non-pre-conditioned PEF or PEF co-polymer preform.

14. The method of claim 11 , wherein surface water on the PEF or PEF co-polymer preform is removed using an air-knife or a fan just prior to stretch blow-molding the pre-conditioned PEF or PEF co-polymer preform.

15. A poly(ethylene furanoate) (PEF) or poly(ethylene furanoate) co-polymer (PEF co-polymer) container made according to claim 11 .

Assignees

• Coca Cola Co

Inventors

• Moffitt Ronald D
• Kriegel Robert
• Schultheis Mikell W
• Shi Yu

Classifications

• B29C49/0005 Primary

  characterised by the material · CPC title

• B29B13/00

  Conditioning or physical treatment of the material to be shaped (chemical aspects C08J3/00 {; heating, cooling or curing during shaping B29C35/00; thermal after-treatment B29C71/02}) · CPC title

• B29K2067/00

  Use of polyesters {or derivatives thereof}, as moulding material · CPC title

• B29K2023/06

  PE, i.e. polyethylene · CPC title

• B29B13/06

  by drying (B29B13/08 takes precedence {; drying moulded articles or half products B29C37/0092}) · CPC title