Granted Patent B2

US 9,023,446 · App. 13/250,189 · Granted May 5, 2015

Abstract

Claims (55)

1. A PET container comprising a wall having a density of between about 1.370 g/cc and 1.385 g/cc, a heat-induced crystallinity of from about 18% to about 25%, and a strain-induced crystallinity of from about 55% to about 75%, wherein the PET container, when filled with a liquid having a temperature of from about 100° C. to about 132° C., will not experience a change in volume of greater than 3%, the container made by a process comprising:

injecting a molten PET resin into an injection mold cavity to form a preform;

removing the preform while the preform is at a temperature of from about 75° C. to about 130° C.;

conveying the preform to at least one conditioning station at a rate such that the temperature of the surface of the preform does not decrease more than 5° C.;

conditioning the preform by selectively heating at least one portion of the preform selected from the group consisting of: neck forming portion, barrel forming portion, base forming portion, and heel forming portion, to define a conditioned preform;

conveying the conditioned preform to a blow mold station at a rate such that the temperature of the surface of the preform does not decrease more than 5° C.;

inserting the conditioned preform into a blow mold having walls that define a blow cavity that defines a shape of a finished article, wherein the mold has at least three temperature zones along an axis of the mold all of which are above the glass transition temperature of PET;

blowing the preform into a finished PET container by a stretch blow molding process comprising the steps of:

i. inserting an elongated stretch blow rod into the conditioned preform to contact a bottom portion of the conditioned preform thereby providing a downward pressure to stretch the conditioned preform to a base portion of the mold;

ii. simultaneously injecting low pressure air into the conditioned preform at a pressure of from about 100 psi to about 200 psi to form a pre-blown preform; and

iii. immediately after ii, injecting high pressure air at a pressure of from about 400 psi to 600 psi into the pre-blown preform to expand the pre-blown preform against the mold walls to form the finished container;

holding the finished container in the mold for a time period of from about 2 seconds to about 20 seconds;

releasing the finished container from the mold wherein the temperature of the finished container is from about 80° C. to about 170° C.; and

allowing the finished container to cool to ambient temperature.

2. A PET container comprising a wall having a density of between about 1.370 g/cc and 1.385 g/cc, a heat-induced crystallinity of from about 18% to about 25%, and a strain-induced crystallinity of from about 55% to about 75%, wherein the PET container, when filled with a liquid having a temperature of from about 100° C. to about 132° C., will not experience a change in volume of greater than 3%, the container made by a process comprising:

injecting a molten PET resin into an injection mold cavity to form a preform;

removing the preform while the preform is at a temperature of from about 75° C. to about 130° C.;

conveying the preform to at least one conditioning station at a rate such that the temperature of the surface of the preform does not decrease more than 5° C.;

conditioning the preform by selectively heating at least one portion of the preform selected from the group consisting of: neck forming portion, barrel forming portion, base forming portion, and heel forming portion, to define a conditioned preform;

conveying the conditioned preform to a first blow mold station at a rate such that the temperature of the surface of the preform does not decrease more than 5° C.;

inserting the conditioned preform into a first blow mold having walls that define a blow cavity that defines a shape of a finished article and a first volume, wherein the first mold has at least three temperature zones along an axis of the first mold all of which are above the glass transition temperature of PET;

blowing the preform into a finished PET container by a stretch blow molding process comprising the steps of:

i. inserting an elongated stretch blow rod into the conditioned preform to contact a bottom portion of the conditioned preform thereby providing a downward pressure to stretch the conditioned preform to a base portion of the first mold;

ii. simultaneously injecting low pressure air into the conditioned preform at a pressure of from about 100 psi to about 200 psi to form a pre-blown preform; and

iii. immediately after ii, injecting high pressure air at a pressure of from about 400 psi to 600 psi into the pre-blown preform to expand the pre-blown preform against the walls of the first mold to form an intermediate container;

iv. holding the intermediate container in the mold for a time period of from about 2 seconds to about 20 seconds;

v. releasing the intermediate container from the mold wherein the temperature of the finished container is from about 80° C. to about 125° C.;

vi. conveying the intermediate container to a second mold having walls that define a blow cavity that defines a shape of a finished article and a second volume, wherein the second mold has at least three temperature zones along an axis of the second mold all of which are above the glass transition temperature of PET, and wherein the second volume is the same as the first volume;

vii. inserting an elongated stretch blow rod into the intermediate container to contact a bottom portion of the intermediate container thereby providing a downward pressure to stretch the intermediate container to a base portion of the second mold and injecting high pressure air at a pressure of from about 400 psi to 600 psi into the intermediate container to expand the intermediate container against the walls of the second mold to form the finished container;

viii. directing a cooling fluid to an inner surface of the finished container;

ix. releasing the finished container from the second mold, wherein the finished container is at a temperature of from about 80° C. to about 170° C.; and

x. allowing the finished container to cool to ambient temperature.

3. A blow-molded PET container comprising a wall having a density of between about 1.370 g/cc and 1.385 g/cc, a heat-induced crystallinity of from about 18% to about 25%, and a strain-induced crystallinity of from about 55% to about 75%, wherein the PET container, when filled with a liquid having a temperature of from about 100° C. to about 132° C., will not experience a change in volume of greater than 3%.

4. The PET container of claim 3 wherein the density of the wall is between about 1.370 g/cc and about 1.375 g/cc.

5. The PET container of claim 3 wherein the density of the wall is greater than about 1.375 g/cc.

6. The PET container of claim 3 wherein the moisture content of the wall is from about 1780 ppm to about 1980 ppm when exposed to 100% RH at about 96° C.

7. The PET container of claim 3 wherein the container is optically clear.

8. The PET container of claim 6 wherein the container is optically clear.

9. The PET container of claim 3 wherein the change in volume is less than 2%.

10. The PET container of claim 9 wherein the change in volume is less than 1%.

11. The PET container of claim 3 wherein the wall, when subjected to temperature modulated differential scanning calorimetry and analyzed in the temperature range of from 0° C. to 325° C. at a heating rate of 5°/min, exhibits a first endothermic glass transition temperature and a second endothermic transition temperature higher than the first transition temperature.

12. The PET container of claim 11 wherein the second endothermic transition temperature is at least 20° C. higher than the first endothermic glass transition temperature.

13. The PET container of claim 12 wherein the second endothermic transition temperature is at least 30° C. higher than the first endothermic glass transition temperature.

14. The PET container of claim 13 wherein the second endothermic transition temperature is at least 40° C. higher than the first endothermic glass transition temperature.

15. The PET container of claim 14 wherein the second endothermic transition temperature is at least 50° C. higher than the first endothermic glass transition temperature.

16. The PET container of claim 11 wherein the second endothermic transition temperature has an enthalpy greater than about 0.5. J/g.

17. The PET container of claim 16 wherein the second endothermic transition temperature has an enthalpy greater than about 1.0. J/g.

18. The PET container of claim 17 wherein the second endothermic transition temperature has an enthalpy greater than about 2.0. J/g.

19. The PET container of claim 3 wherein the wall of the container has a moisture content of from about 1850 ppm to about 1930 ppm when exposed to ambient conditions for 4 days.

20. The PET container of claim 3 wherein, when subjected to X-ray diffraction analysis over a range of 10° to 70° with a step size of 0.0158° and a counting time of 250 seconds per step, an X-ray diffraction pattern exhibits at least five crystalline peaks.

21. The PET container of claim 20 wherein the X-ray diffraction pattern exhibits at least six crystalline peaks.

22. The PET container of claim 20 wherein one of the peaks is at 17.44° and another of the peaks is at 42.25°.

23. The container of claim 1 wherein the temperature of the liquid is selected from the group consisting of 115.5° C., 126.6° C., and 137° C.

24. The container of claim 2 wherein the temperature of the liquid is selected from the group consisting of 115.5° C., 126.6° C., and 137° C.

25. The container of claim 3 wherein the temperature of the liquid is selected from the group consisting of 115.5° C., 126.6° C., and 137° C.

Assignments (7)