IP Library Granted Patent US 10,071,895
Granted Patent B2
US 10,071,895 · App. 14/965,098 · Granted Sep 11, 2018

Hot fill process with closures made from high density unimodal polyethylene

Inventors: XiaoChuan Wang (Calgary, CA); Mark Rejman (Barrie, CA); Ronald William Lewoniuk (Rocky View County, CA); Ian Robert Gibbons (Calgary, CA); Eric Paul Brusset (Calgary, CA)
Assignee: NOVA Chemicals (International) S.A.
B67C3/22B65D41/04B67B6/00B67C3/045B67C2003/228
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Quick Facts
Patent No.
US 10,071,895
App. No.
14/965,098
Granted
Sep 11, 2018
Kind
B2
Abstract

High density (density ≥0.945 g/cm 3 ) unimodal polyethylene compositions for use in hot-fill closures and processes.

Claims (44)

1. A process to fill a container, the process comprising: adding a hot liquid to the container through a container opening, sealing the container opening with a closure comprising a unimodal polyethylene composition, and bringing the hot liquid into contact with an interior surface of the closure; wherein the unimodal polyethylene composition has a density from 0.945 to 0.967 g/cm 3 ; a melt index, I 2 of from 2.5 to 20.0 g/10 min; a weight average molecular weight (Mw) from 25,000 to 85,000 g/mol; and a molecular weight distribution M w /M n of from 2.2 to 4.2.

2. The process of claim 1 wherein the unimodal polyethylene composition is an ethylene homopolymer.

3. The process of claim 2 wherein the unimodal polyethylene composition has a density of from 0.958 to 0.963 g/cm 3 .

4. The process of claim 3 wherein the unimodal polyethylene composition has a melt index, I 2 of from 3.0 to 12.0 g/10 min.

5. The process of claim 2 wherein the unimodal polyethylene composition has a melt index, I 2 of from 3.0 to 12.0 g/10 min.

6. The process of claim 1 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin.

7. The process of claim 6 wherein the unimodal polyethylene composition has a density of from 0.948 to 0.958 g/cm 3 .

8. The process of claim 7 wherein the unimodal polyethylene composition has a melt index, I 2 of from 4.0 to 20.0 g/10 min.

9. The process of claim 8 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin selected from 1-butene, 1-hexene and 1-octene.

10. The process of claim 7 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin selected from 1-butene, 1-hexene and 1-octene.

11. The process of claim 6 wherein the unimodal polyethylene composition has a melt index, I 2 of from 4.0 to 20.0 g/10 min.

12. The process of claim 11 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin selected from 1-butene, 1-hexene and 1-octene.

13. The process of claim 6 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin selected from 1-butene, 1-hexene and 1-octene.

14. The process of claim 1 wherein the unimodal polyethylene composition further comprises a nucleating agent or a mixture of nucleating agents.

15. The process of claim 1 wherein the unimodal polyethylene composition is prepared by contacting ethylene and optionally an alpha-olefin with a polymerization catalyst under solution polymerization conditions.

16. The process of claim 1 wherein the closure is made by continuous compression molding or injection molding.

17. The process of claim 1 wherein the unimodal polyethylene composition is made with a Ziegler-Natta catalyst.

18. The process of claim 1 wherein the unimodal polyethylene composition has less than 0.8 ppm of titanium present.

19. The process of claim 1 wherein the unimodal polyethylene composition has an ESCR Condition B (10% IGEPAL) of at least 1 hour.

20. Use of a closure in a hot fill process, wherein the closure comprises a unimodal polyethylene composition having a density from 0.945 to 0.967 g/cm 3 ; a melt index, I 2 of from 2.5 to 20.0 g/10 min; a weight average molecular weight (Mw) from 25,000 to 85,000 g/mol; and a molecular weight distribution M w /M n of from 2.2 to 4.2.

21. The use according to claim 20 wherein the unimodal polyethylene composition is a homopolymer.

22. The use according to claim 21 wherein the unimodal polyethylene composition has a density of from 0.958 to 0.963 g/cm 3 .

23. The use according to claim 22 wherein the unimodal polyethylene composition has a melt index, I 2 of from 3.0 to 12.0 g/10 min.

24. The use according to claim 21 wherein the unimodal polyethylene composition has a melt index, I 2 of from 3.0 to 12.0 g/10 min.

25. The use according to claim 20 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin.

26. The use according to claim 25 wherein the unimodal polyethylene composition has a density of from 0.948 to 0.958 g/cm 3 .

27. The use according to claim 26 wherein the unimodal polyethylene composition has a melt index, I 2 of from 4.0 to 20.0 g/10 min.

28. The use according to claim 27 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin selected from 1-butene, 1-hexene and 1-octene.

29. The use according to claim 26 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin selected from 1-butene, 1-hexene and 1-octene.

30. The use according to claim 25 wherein the unimodal polyethylene composition has a melt index, I 2 of from 4.0 to 20.0 g/10 min.

31. The use according to claim 30 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin selected from 1-butene, 1-hexene and 1-octene.

32. The use according to claim 25 wherein the unimodal polyethylene composition is a copolymer of ethylene and an alpha olefin selected from 1-butene, 1-hexene and 1-octene.

33. The use according to claim 20 wherein the unimodal polyethylene composition further comprises a nucleating agent or a mixture of nucleating agents.

34. The use according to claim 20 wherein the unimodal polyethylene composition is prepared by contacting ethylene and optionally an alpha-olefin with a polymerization catalyst under solution polymerization conditions.

35. The use according to claim 20 wherein the closure is made by continuous compression molding or injection molding.

36. The use according to claim 20 wherein the unimodal polyethylene composition is made with a Ziegler-Natta catalyst.

37. The use according to claim 20 wherein the unimodal polyethylene composition has less than 0.8 ppm of titanium present.

38. The use according to claim 20 wherein the unimodal polyethylene composition has an ESCR Condition B (10% IGEPAL) of at least 1 hour.

39. A process to fill a container, the process comprising: adding a hot liquid to the container through a container opening; sealing the container opening with a closure comprising a unimodal polyethylene composition having a density from 0.945 to 0.967 g/cm 3 ; a melt index, I 2 of from 2.5 to 20.0 g/10 min; a weight average molecular weight (Mw) from 25,000 to 85,000 g/mol; and a molecular weight distribution M w /M n of from 2.2 to 4.2; and bringing the hot liquid into contact with an interior surface of the closure; wherein the closure has a time exponent, m of 0.114 or less where m is determined using a compressive strain model represented by the equation:

ε= A×σ n ×t m

where ε is the compressive strain; σ is the stress in N/cm 2 , t is the loading time in seconds, A is the model coefficient, n is the deformation stress exponent and m is the time exponent.

40. Use of a closure in a hot fill process, wherein the closure comprises a unimodal polyethylene composition having a density from 0.945 to 0.967 g/cm 3 ; a melt index, I 2 of from 2.5 to 20.0 g/10 min; a weight average molecular weight (Mw) from 25,000 to 85,000 g/mol; a molecular weight distribution M w /M n of from 2.2 to 4.2; wherein the closure has a time exponent, m of 0.114 or less, where m is determined using a compressive strain model represented by the equation:

ε= A×σ n ×t m

where ε is the compressive strain; σ is the stress in N/cm 2 , t is the loading time in seconds, A is the model coefficient, n is the deformation stress exponent and m is the time exponent.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 11, 2016
From: WANG, XIAOCHUAN; REJMAN, MARK; LEWONIUK, RONALD WILLIAM; GIBBONS, IAN ROBERT; BRUSSET, ERIC PAUL
To: NOVA CHEMICALS (INTERNATIONAL) S.A.
Reel/Frame 037704/0922 →
Priority Claims (1)
CA 2914315 · Dec 9, 2015 · national
Continuity (1)
Related Publication 20170166430A1 · Jun 15, 2017
Cited By (2)
US 12,486,345 US 12,491,678