IP Library Granted Patent US 7,045,556
Granted Patent B2
US 7,045,556 · App. 10/188,263 · Granted May 16, 2006

Polyolefin foams made with isopentane-based blowing agents

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Quick Facts
Patent No.
US 7,045,556
App. No.
10/188,263
Granted
May 16, 2006
Kind
B2
Abstract

A blowing agent blend for making polyolefin foams comprising isopentane and at least one co-blowing agent. The co-blowing agent is either a physical co-blowing agent having a boiling point less than 28° C., or a chemical co-blowing agent, or combinations thereof. The blowing agent blend comprises less than about 99 mol % isopentane.

Claims (92)

1. A blowing agent blend for making polyolefin foams comprising isopentane and at least one co-blowing agent, the co-blowing agent being (i) a physical co-blowing agent having a boiling point less than 28° C., (ii) a chemical co-blowing agent, or (iii) combinations thereof, and

wherein the blowing agent blend comprises less than about 99 mol % isopentane, and wherein if one of the at least one co-blowing agent is a physical co-blowing agent being isobutane, the blowing agent blend comprises less than 70 mol % isobutane.

2. The blowing agent blend of claim 1 , wherein the polyolefin foam is dimensionally stable.

3. The blowing agent blend of claim 1 , wherein the co-blowing agent includes at least one physical co-blowing agent, the at least one physical co-blowing agent being methane, ethane, n-propane, n-butane, isobutane, cyclopropane, nitrogen, argon, carbon dioxide, sulfur hexafluoride, nitrous oxide, dimethyl ether, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroet (HFC-134), 1,1,1,3,3-pentafluoropropane (HFC-245fa), or combinations thereof.

4. The blowing agent blend of claim 1 , wherein the blowing agent blend includes a chemical co-blowing agent.

5. The blowing agent blend of claim 1 , wherein the blowing agent blend comprises from about 10 mol % to about 60 mol % isopentane.

6. The blowing agent blend of claim 5 , wherein the blowing agent blend comprises from about 15 mol % to about 40 mol % isopentane.

7. The blowing agent blend of claim 6 , wherein the blowing agent blend comprises from about 25 mol % to about 40 mol % isopentane.

8. The blowing agent blend of claim 1 , wherein the polyolefin foam comprises polyethylene.

9. The blowing agent blend of claim 1 , wherein the polyolefin foam has a density of less than 3 lb/ft 3 .

10. A polyolefin foam structure prepared by the process comprising the acts of:

melting a thermoplastic polyolefin polymer;

dissolving an effective amount of a blowing agent blend in the polyolefin polymer, the blowing agent blend comprising isopentane and at least one co-blowing agent, the co-blowing agent being (i) a physical co-blowing agent having a boiling point less than 28° C., (ii) a chemical co-blowing agent, or (iii) combinations thereof, and wherein the blowing agent blend comprises less than about 99 mol % isopentane, and wherein if one of the at least one co-blowing agent is a physical co-blowing agent being isobutane, the blowing agent blend comprises less than 70 mol % isobutane;

forming an extrudate;

transferring the extrudate to an expansion zone; and

permitting the extrudate to expand in the expansion zone to produce the polyolefin foam structure, the polyolefin foam structure being a substantially closed-cell and dimensionally-stable structure.

11. The polyolefin foam structure of claim 10 , wherein the extrudate comprises from about 1 to about 18 wt % blowing agent.

12. The polyolefin foam structure of claim 10 , wherein the polyolefin foam structure has at least 20 cells per inch.

13. The polyolefin foam structure of claim 12 , wherein the polyolefin foam structure has at least 25 cells per inch.

14. The polyolefin foam structure of claim 13 , wherein the polyolefin foam structure has at least 30 cells per inch.

15. The polyolefin foam structure of claim 10 , wherein the polyolefin foam structure is a sheet.

16. The polyolefin foam structure of claim 10 , wherein the polyolefin foam structure is a plank.

17. The polyolefin foam structure of claim 10 further including mixing a nucleating agent and the thermoplastic polyolefin polymer to form a mixture, and dissolving an effective amount of the blowing agent blend into the mixture.

18. The polyolefin foam structure of claim 10 further including

melting a stability control agent,

mixing the stability control agent and the thermoplastic polyolefin polymer to form a mixture, and

dissolving an effective amount of the blowing agent blend into the mixture.

19. The polyolefin foam structure of claim 10 , wherein the polyolefin foam structure comprises polyethylene.

20. The polyolefin foam structure of claim 19 , wherein the polyolefin foam structure comprises low density polyethylene.

21. The polyolefin foam structure of claim 10 , wherein the polyolefin foam structure has a density of less than 3 lb/ft 3 .

22. A process for making a polyolefin foam structure comprising the acts of:

melting a thermoplastic polyolefin polymer;

dissolving an effective amount of a blowing agent blend in the polyolefin polymer, the blowing agent blend comprising isopentane and at least one co-blowing agent, the co-blowing agent being (i) a physical co-blowing agent having a boiling point less than 28° C., (ii) a chemical co-blowing agent, or (iii) combinations thereof, and wherein the blowing agent blend comprises less than about 99 mol % isopentane, and wherein if one of the at least one co-blowing agent is a physical co-blowing agent being isobutane, the blowing agent blend comprises less than 70 mol % isobutane;

forming an extrudate;

transferring the extrudate to an expansion zone; and

permitting the extrudate to expand in the expansion zone to produce the polyolefin foam structure.

23. The process of claim 22 , wherein the polyolefin structure is a substantially closed-cell and dimensionally stable structure.

24. The process of claim 22 , wherein the extrudate comprises from about 1 to about 18 wt % blowing agent.

25. The process of claim 22 further including mixing a nucleating agent and the thermoplastic polyolefin polymer to form a mixture, and dissolving an effective amount of the blowing agent blend into the mixture.

26. The process of claim 22 further including

melting a stability control agent,

mixing the stability control agent and the thermoplastic polyolefin polymer to form a mixture, and

dissolving an effective amount of the blowing agent blend into the mixture.

27. The process of claim 22 , wherein the co-blowing agent includes at least one physical co-blowing agent, the at least one physical co-blowing agent being methane, ethane, n-propane, n-butane, isobutane, cyclopropane, nitrogen, argon, carbon dioxide, sulfur hexafluoride, nitrous oxide, dimethyl ether, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,3,3-pentafluoropropane (HFC-245fa), or combinations thereof.

28. The process of claim 22 , wherein the blowing agent blend includes a chemical co-blowing agent.

29. The process of claim 22 , wherein the blowing agent blend comprises from about 10 mol % to about 60 mol % isopentane.

30. The process of claim 29 , wherein the blowing agent blend comprises from about 15 mol % to about 40 mol % isopentane.

31. The process of claim 30 , wherein the blowing agent blend comprises from about 25 mol % to about 40 mol % isopentane.

32. The process of claim 22 , wherein the polyolefin foam structure comprises polyethylene.

33. The process of claim 32 , wherein the polyolefin foam structure comprises low density polyethylene.

34. The process of claim 22 , wherein the polyolefin foam structure has a density of less than 3 lb/ft 3 .

35. A blowing agent blend for foaming low density polyethylene foam consisting essentially of from about 10 to about 99 mol % isopentane and at least one co-blowing agent, the co-blowing agent being (i) a physical co-blowing agent having a boiling point less than 28° C., (ii) a chemical co-blowing agent, or (iii) combinations thereof, and wherein if one of the at least one co-blowing agent is a physical co-blowing agent being isobutane, the blowing agent blend comprises less than 70 mol % isobutane.

36. The blowing agent blend of claim 35 , wherein the co-blowing agent includes at least one physical co-blowing agent, the at least one physical co-blowing agent being methane, ethane, n-propane, n-butane, isobutane, cyclopropane, nitrogen, argon, carbon dioxide, sulfur hexafluoride, nitrous oxide, dimethyl ether, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,3,3-pentafluoropropane (HFC-245fa), or combinations thereof.

37. The blowing agent blend of claim 35 , wherein the blowing agent blend comprises from about 10 mol % to about 60 mol % isopentane.

38. The blowing agent blend of claim 37 , wherein the blowing agent blend comprises from about 25 mol % to about 40 mol % isopentane.

39. A process for making a low density polyethylene foam structure prepared by the process comprising the acts of:

melting a low density polyethylene polymer;

dissolving an effective amount of a blowing agent blend in the low density polyethylene polymer, the blowing agent blend comprising from about 10 to about 99 mol % isopentane and at least one co-blowing agent, the co-blowing agent being (i) a physical co-blowing agent having a boiling point less than 28° C., (ii) a chemical co-blowing agent, or (iii) combinations thereof, and wherein if one of the at least one co-blowing agent is a physical co-blowing agent being isobutane, the blowing agent blend comprises less than 70 mol % isobutane;

forming an extrudate;

transferring the extrudate to an expansion zone; and

permitting the extrudate to expand in the expansion zone to produce the low density polyethylene structure.

40. The process of claim 39 further including

melting a stability control agent,

mixing a nucleating agent, the stability control agent and the thermoplastic polyolefin polymer to form a mixture, and

dissolving an effective amount of the blowing agent blend into the mixture.

41. The process of claim 40 , wherein the nucleating agent is talc, and the stability control agent is glycerol monostearate.

42. The process of claim 39 , wherein the co-blowing agent includes at least one physical co-blowing agent, the at least one physical co-blowing agent being methane, ethane, n-propane, n-butane, isobutane, cyclopropane, nitrogen, argon, carbon dioxide, sulfur hexafluoride, nitrous oxide, dimethyl ether, 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,3,3-pentafluoropropane (HFC-245fa), or combinations thereof.

43. The process of claim 39 , wherein the blowing agent blend includes a chemical co-blowing agent.

44. The process of claim 39 , wherein the blowing agent blend comprises from about 10 mol % to about 60 mol % isopentane.

45. The process of claim 44 , wherein the blowing agent blend comprises from about 25 mol % to about 40 mol % isopentane.

46. The process of claim 39 , wherein the low density polyethylene foam has a density of less than 3 lb/ft 3 .

47. The blowing agent blend of claim 1 , wherein the blowing agent blend comprises isopentane and isobutane, the blowing agent comprises less than 70 mol % isobutane.

48. The blowing agent blend of claim 47 , wherein the blowing agent blend further includes at least one additional co-blowing agent selected from the group consisting of methane, ethane, n-propane, cyclopropane, and n-butane.

49. The blowing agent blend of claim 1 , wherein the blowing agent blend comprises less than 99 mol % isopentane and (i) at least one physical co-blowing hydrocarbon agent having a boiling point less than 28° C. and the at least one physical co-blowing hydrocarbon agent not being isobutane, (ii) at least one physical non-hydrocarbon co-blowing agent having a boiling point less than 28° C., (iii) at least one chemical co-blowing agent, or (iv) combinations thereof.

50. The blowing agent blend of claim 49 , wherein the blowing agent blend comprises less than 99 mol % isopentane and at least one physical hydrocarbon co-blowing agent selected from the group consisting of methane, ethane, n-propane, cyclopropane, and n-butane.

51. The blowing agent blend of claim 1 , wherein the blowing agent blend comprises less than 99 mol % isopentane and at least one physical non-hydrocarbon co-blowing agent having a boiling point less than 28° C.

52. The process of claim 22 , wherein the blowing agent blend comprises isopentane and isobutane, the blowing agent comprises less than 70 mol % isobutane.

53. The process of claim 52 , wherein the blowing agent blend further includes at least one additional co-blowing agent selected from the group consisting of methane, ethane, n-propane, cyclopropane, and n-butane.

54. The process of claim 22 , wherein the blowing agent blend comprises less than 99 mol % isopentane and (i) at least one physical co-blowing hydrocarbon agent having a boiling point less than 28° C. and the at least one physical co-blowing hydrocarbon agent not being isobutane, (ii) at least one physical non-hydrocarbon co-blowing agent having a boiling point less than 28° C., (iii) at least one chemical co-blowing agent, or (iv) combinations thereof.

55. The process of claim 54 , wherein the blowing agent blend comprises less than 99 mol % isopentane and at least one physical hydrocarbon co-blowing agent selected from the group consisting of methane, ethane, n-propane, cyclopropane, and n-butane.

56. The process of claim 22 , wherein the blowing agent blend comprises less than 99 mol % isopentane and at least one physical non-hydrocarbon co-blowing agent having a boiling point less than 28° C.

57. A blowing agent blend for making polyolefin foams comprising (i) isopentane, (ii) isobutane, and (iii) at least one of the co-blowing agents selected from the group consisting of n-propane, 1,1,1,2-tetrafluoroethane (HFC-134a), dimethyl ether, ethane, butane, and combinations thereof, and wherein the blowing agent blend comprises less than 70 mol % isobutane.

58. The blowing agent blend of claim 57 , wherein the blowing agent blend consists essentially of (i) isopentane, (ii) isobutane, and (iii) at least one of the co-blowing agents selected from the group consisting of n-propane, 1,1,1,2-tetrafluoroethane (HFC-134a), dimethyl ether, and combinations thereof.

59. The blowing agent blend of claim 57 , wherein the blowing agent blend comprises at least 10 mol % isopentane.

60. A process for making a polyolefin foam structure comprising the acts of:

melting a thermoplastic polyolefin polymer;

dissolving an effective amount of a blowing agent blend in the polyolefin polymer, the blowing agent blend comprising (i) isopentane, (ii) isobutane, and (iii) at least one of the co-blowing agents selected from the group consisting of n-propane, 1,1,1,2-tetrafluoroethane (HFC-134a), dimethyl ether, ethane, butane, and combinations thereof, and wherein the blowing agent blend comprises less than 70 mol % isobutane;

forming an extrudate;

transferring the extrudate to an expansion zone; and

permitting the extrudate to expand in the expansion zone to produce the polyolefin foam structure.

61. The process of claim 60 , wherein the blowing agent blend consists essentially of (i) isopentane, (ii) isobutane, and (iii) at least one of the co-blowing agents selected from the group consisting of n-propane, 1,1,1,2-tetrafluoroethane (HFC-134a), dimethyl ether, and combinations thereof.

62. The process of claim 60 , wherein the blowing agent blend comprises at least 10 mol % isopentane.

Assignments (11)
ASSIGNMENT OF PATENT SECURITY INTERESTS (FIRST LIEN) Recorded Aug 8, 2024
From: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH
To: UBS AG, STAMFORD BRANCH, AS SUCCESSOR AGENT
Reel/Frame 068518/0568 →
RELEASE OF SECURITY INTEREST Recorded Nov 13, 2019
From: OWL ROCK CAPITAL CORPORATION, AS COLLATERAL AGENT
To: PREGIS INNOVATIVE PACKAGING INC.; PREGIS INTELLIPACK LLC; PREGIS SHARP SYSTEMS, LLC; FREE-FLOW PACKAGING INTERNATIONAL, INC.
Reel/Frame 050993/0798 →
FIRST LIEN SECURITY AGREEMENT Recorded Aug 1, 2019
From: PREGIS INNOVATIVE PACKAGING LLC
To: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH
Reel/Frame 049932/0377 →
SECOND LIEN PATENT SECURITY AGREEMENT Recorded Aug 1, 2019
From: PREGIS INNOVATIVE PACKAGING LLC
To: OWL ROCK CAPITAL CORPORATION, AS SECOND LIEN COLLATERAL AGENT
Reel/Frame 049941/0652 →
CHANGE OF NAME Recorded Jul 18, 2019
From: PREGIS INNOVATIVE PACKAGING INC.
To: PREGIS INNOVATIVE PACKAGING LLC
Reel/Frame 049869/0050 →
SECURITY INTEREST Recorded Jul 19, 2018
From: PREGIS INNOVATIVE PACKAGING INC.; PREGIS INTELLIPACK LLC; PREGIS SHARP SYSTEMS, LLC; FREE-FLOW PACKAGING INTERNATIONAL, INC.
To: OWL ROCK CAPITAL CORPORATION, AS COLLATERAL AGENT
Reel/Frame 046593/0535 →
CORRECTIVE ASSIGNMENT TO CORRECT THE PATENT NUMBER 6477534 PREVIOUSLY RECORDED AT REEL: 028109 FRAME: 0947. ASSIGNOR(S) HEREBY CONFIRMS THE RELEASE OF SECOND LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT. Recorded Nov 26, 2014
From: BANK OF NEW YORK MELLON TRUST COMPANY N.A. (AS SUCCESSOR TO THE BANK OF NEW YORK)
To: PREGIS HOLDING II CORPORATION; PREGIS CORPORATION; PREGIS INNOVATIVE PACKAGING, INC.; PREGIS INTELLIPACK CORP.
Reel/Frame 034566/0635 →
RELEASE OF SECURITY INTEREST Recorded May 21, 2014
From: GENERAL ELECTRIC CAPITAL CORPORATION
To: PREGIS INNOVATIVE PACKAGING INC.
Reel/Frame 032971/0256 →
RELEASE OF SECURITY INTEREST Recorded May 21, 2014
From: WELLS FARGO BANK, NATIONAL ASSOCIATION
To: PREGIS INNOVATIVE PACKAGING INC.
Reel/Frame 032971/0280 →
RELEASE OF SECOND LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded Apr 26, 2012
From: THE BANK OF NEW YORK MELLON TRUST COMPANY N.A. (AS SUCCESSOR TO THE BANK OF NEW YORK)
To: PREGIS HOLDING II CORPORATION; PREGIS CORPORATION; PREGIS INNOVATIVE PACKAGING, INC.; PREGIS INTELLIPACK CORP.
Reel/Frame 028109/0947 →
PATENT SECURITY AGREEMENT Recorded Mar 23, 2011
From: PREGIS HOLDING II CORPORATION; PREGIS CORPORATION; PREGIS INNOVATIVE PACKAGING INC.; PREGIS INTELLIPACK CORP.; HEXACOMB CORPORATION
To: WELLS FARGO CAPITAL FINANCE, LLC, AS AGENT
Reel/Frame 026010/0305 →