PET Polymer with Improved Properties

Abstract

Polyester compositions having desirable injection molding properties and that retain good crystallization rates and natural stretch ratio characteristics are described. These polyesters are suitable for the manufacture of beverage containers, bulk continuous filaments, and other articles that can benefit from such improved properties.

Description

CROSS-REFERENCE TO RELATED APPLICATION[0001]This application is a continuation of application Ser. No. 11 / 254,407, entitled “PET Polymers With Improved Properties” which was filed on Oct. 20, 2005, all of which is hereby incorporated by this reference in its entirety.FIELD OF THE INVENTION[0002]The present invention is directed to certain polyesters having desirable injection molding properties while retaining good crystallization rates and natural stretch ratio characteristics. These polyesters may be advantageously used, for example, in water applications, for instance, for the manufacture of beverage containers. These polyesters can also be used in the manufacture of bulk continuous filaments, and other articles that can benefit from such properties.BACKGROUND[0003]Poly(ethylene terephthalate) copolymers, commonly referred to as PET polymers, are widely used in the manufacture of light weight containers for carbonated and non-carbonated drinks, juice, water, jellies, marmalades, ...

AI Technical Summary

Benefits of technology

[0069]The polyesters of the present invention typically contain a lower mole percent of diethylene glycol (DEG) than many other polyesters used in similar applications. Any method suitable for reducing DEG content of polyester can be employed in the present invention. Suitable methods include reducing the mole ratio of diacid or diester relative to ethylene glycol in the esterification or transesterification reaction; reducing the temperature of the esterification or transesterification reaction, addition of DEG-suppressing additives, including tetra-alkyl ammonium salts and the like; and reduction of the DEG content of the ethylene glycol that is recycled back to the esterification or transesterification reaction.

[0070]In certain embodiments, the polyesters of the invention comprise less than 2.0 mol % of diethylene glycol or less than 1.6 mol % of diethylene glycol. The minimization of the DEG content allows for substitution with comonomers that could be more effective in retarding the crystallization rate or provide other beneficial characteristic to the polyester. In this manner, the total amount of comonomer modification employed can be reduced.

[0072]We have found that minimizing the DEG content and maintaining the molar ratios of comonomer to DEG mentioned above allows a reduction in the pellet intrinsic viscosity while maintaining desirable natural stretch ratio and container physical properties. A reduction in the pellet inherent viscosity is valuable in a number of ways. A lower viscosity resin will fill the injection mold more easily, leading to a reduction in injection molding cycle time and an increase in product output. Also, a lower viscosity resin will reduce the injection pressure required to fill the mold in a given time, reducing the wear and tear on the injection molding machine. Therefore, manufacturing costs may be reduced for resins with a lower intrinsic viscosity.

[0077]Acetaldehyde content can be successfully reduced in crystalline PET compositions by solid state polymerization. Solid state polymerization of PET polymers not only decreases its acetaldehyde content but also decreases its tendency to form acetaldehyde. Additionally, polyamides or other acetaldehyde scavengers known in the art can be used to reduce the level of acetaldehyde to an acceptable range.

[0085]The present invention also provides a process for making a polyester container, for example a preform or a beverage bottle, comprising feeding crystallized polyester particles or pellets of the invention to an extrusion zone, melting the particles in the extrusion zone to form a molten polyester polymer composition, and forming a sheet or a molded part from extruded molten polyester polymer. The particles fed to the extrusion zone are normally dried and typically have sufficient crystallinity to prevent them from sticking to each other or to equipment during drying at a temperature ranging from 140° C. to 180° C. Moreover, the crystallized polyester particles fed to the extrusion zone after drying can contain low levels of residual acetaldehyde (as measured by the French National Standard Test), such as 10 ppm or less, 5 ppm or less, 2 ppm or less, or even 1 ppm or less. The sheet or molded part can be further processed to make thermoformed or blowmolded containers.

Problems solved by technology

Due to the high cost of injection mold tooling, new PET resins that perform well with existing preform designs can be used.

Resins with very low natural stretch ratios generally create processing problems during stretch blow molding, while resins with very high natural stretch ratios generally yield containers with poor physical properties if used in conjunction with preform and bottle tooling.

Thermally induced crystallization tends to form large crystallites in the polymer, resulting in haze.

However, if the rate of thermal crystallization is too low, the production rates of PET resin using solid state polymerization can be adversely affected because PET needs to be crystallized prior to solid-state polymerization.

Unfortunately, improving one of these three properties—natural stretch ratio, crystallization rate, or fill injection rate—has normally resulted in detriment to one or both of the remaining properties.

For example, compositions with suitably slow crystallization rates often require a higher intrinsic viscosity to maintain an adequate natural stretch ratio, which adversely impacts the fill time in injection molding.