IP Library Granted Patent US 9,181,421
Granted Patent B2
US 9,181,421 · App. 14/205,678 · Granted Nov 10, 2015

High-density polyethylene compositions, method of making the same

Inventors: William J. Michie, Jr. (Missouri City, TX); Thomas W. Kay (Scott Depot, WV); Stephanie M. Whited (Charleston, WV); Dale M. Elley-Bristow (Sarnia, CA); David T. Gillespie (Pearland, TX); Lonnie G. Hazlitt (Lake Jackson, TX)
Assignee: Dow Global Technologies LLC
C08L23/08C08L23/04C08L23/06C08L23/0815C08L2203/10Y10T428/24992Y10T428/273
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Quick Facts
Patent No.
US 9,181,421
App. No.
14/205,678
Granted
Nov 10, 2015
Kind
B2
Abstract

The instant invention is a high-density polyethylene composition, method of producing the same, articles made therefrom, and method of making such articles. The high-density polyethylene composition of the instant invention includes a first component, and a second component. The first component is a high molecular weight ethylene alpha-olefin copolymer having a density in the range of 0.915 to 0.940 g/cm 3 , and a melt index (I 21.6 ) in the range of 0.5 to 10 g/10 minutes. The second component is a low molecular weight ethylene polymer having a density in the range of 0.965 to 0.980 g/cm 3 , and a melt index (I 2 ) in the range of 50 to 1500 g/10 minutes. The high-density polyethylene composition has a melt index (I 2 ) of at least 1, a density in the range of 0.950 to 0.960 g/cm 3 , and g′ of 1.

Claims (26)

1. A method of producing a high-density polyethylene composition comprising the steps of:

introducing ethylene, and an alpha-olefin comonomer into a first reactor;

polymerizing said ethylene in the presence of said alpha-olefin comonomer in said first reactor thereby producing a first component, wherein said first component being a high molecular weight ethylene alpha-olefin copolymer having a density in the range of 0.915 to 0.940 g/cm 3 , and a melt index (I 21 ) in the range of 0.5 to 10 g/10 minutes;

introducing said first component and additional ethylene into a second reactor;

polymerizing said additional ethylene in said second reactor thereby producing a second component, wherein said second component being a low molecular weight ethylene polymer having a density in the range of 0.965 to 0.980 g/cm 3 , and a melt index (I 2 ) in the range of 50 to 1500 g/10 minutes; and

thereby producing said high-density polyethylene composition, wherein high-density polyethylene composition having a melt index (I 2 ) of at least 1 g/10 minutes, a density in the range of 0.950 to 0.960 g/cm 3 , and g′ of equal or greater than 1.

2. The method of producing a high-density polyethylene composition according to claim 1 , wherein said first component having a density in the range of 0.920 to 0.940 g/cm 3 .

3. The method of producing a high-density polyethylene composition according to claim 1 , wherein said first component having a density in the range of 0.921 to 0.936 g/cm 3 .

4. The method of producing a high-density polyethylene composition according to claim 1 , wherein said first component having a melt index (I 21.6 ) in the range of 1 to 7 g/10 minutes.

5. The method of producing a high-density polyethylene composition according to claim 1 , wherein said first component having a melt index (I 21.6 ) in the range of 1.3 to 5 g/10 minutes.

6. The method of producing a high-density polyethylene composition according to claim 1 , wherein said second component having a density in the range of 0.970 to 0.975 g/cm 3 .

7. The method of producing a high-density polyethylene composition according to claim 1 , wherein said second component having a melt index (I 2 ) in the range of 100 to 1500 g/10 minutes.

8. The method of producing a high-density polyethylene composition according to claim 1 , wherein said second component having a melt index (I 2 ) in the range of 200 to 1500 g/10 minutes.

9. The method of producing a high-density polyethylene composition according to claim 1 , wherein said high-density polyethylene composition having a melt index (I 2 ) in the range of 1 to 2 g/10 minutes.

10. The method of producing a high-density polyethylene composition according to claim 1 , wherein said high-density polyethylene composition having a melt index (I 2 ) of at least 2 g/10 minutes.

11. The method of producing a high-density polyethylene composition according to claim 1 , wherein said first component having a molecular weight in the range of 150,000 to 375,000.

12. The method of producing a high-density polyethylene composition according to claim 1 , wherein said second component having a molecular weight in the range of 12,000 to 40,000.

13. The method of producing a high-density polyethylene composition according to claim 1 , wherein said first component having a density in the range of 0.921 to 0.936 g/cm 3 , and a melt index (I 21.6 ) in the range of 1.3 to 5 g/10 minutes; wherein said second component having a density in the range of 0.970 to 0.975 g/cm 3 , and a melt index (I 2 ) in the range of 200 to 1500 g/10 minutes.

14. The method of producing a high-density polyethylene composition according to claim 1 , wherein said first component being substantially free of any long chain branching, and said second component being substantially free of any long chain branching.

15. The method of producing a high-density polyethylene composition according to claim 14 , wherein said high-density polyethylene composition being substantially free of any long chain branching.

16. The method of producing a high-density polyethylene composition according to claim 1 , wherein said high-density polyethylene composition having a single ATREF temperature peak, wherein said ATREF temperature peak having a temperature peak maximum between 90° C. to 105° C.;

wherein said high-density polyethylene composition having a calculated high density fraction in the range of 20 percent to 50 percent, said calculated high density fraction being defined as [(2)*(the weight ratio of the high-density polyethylene that elutes in ATREF-DV at temperatures greater than or equal to said temperature peak maximum)],

wherein said high-density polyethylene composition having a relative minimum in the log of the relative viscosity average molecular weight at about 90° C. in ATRF-DV;

wherein said high-density polyethylene composition having a regression slope of the log of the relative viscosity average molecular weight versus the ATREF-DV viscosity versus temperature plot of less than about 0, said elution temperature measured between 70° C. to 90° C.

17. The method of producing a high-density polyethylene composition according to claim 1 , wherein said high-density polyethylene composition having a comonomer content in weight percent of equal or greater that [(−228.41*density of said high-density polyethylene composition)+219.36)]*[1(weight percent)/(g/cm 3 )], wherein the density being measured in g/cm 3 .

18. The method of producing a high-density polyethylene composition according to claim 1 , wherein said high-density polyethylene composition having an ATREF high-density fraction in percent of equal or less than [(2750*density of the high-density polyethylene composition)−2552.2]*[1(percent)/(g/cm 3 )], where the density being measured in g/cm 3 .

Assignments (7)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: ELLEY-BRISTOW, DALE M.
To: DOW CHEMICAL CANADA INC.
Reel/Frame 033107/0990 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: DOW CHEMICAL CANADA INC.
To: THE DOW CHEMICAL COMPANY
Reel/Frame 033108/0025 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: THE DOW CHEMICAL COMPANY
To: DOW GLOBAL TECHNOLOGIES INC.
Reel/Frame 033108/0045 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: MICHIE, WILLIAM J., JR.; GILLESPIE, DAVID T.; HAZLITT, LONNIE G.
To: DOW GLOBAL TECHNOLOGIES INC.
Reel/Frame 033108/0117 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: KAY, THOMAS W.; WHITED, STEPHANIE M.
To: UNION CARBIDE CHEMICALS & PLASTICS TECHNOLOGY CORPORATION
Reel/Frame 033108/0147 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: UNION CARBIDE CHEMICALS & PLASTICS TECHNOLOGY CORPORATION
To: DOW GLOBAL TECHNOLOGIES INC.
Reel/Frame 033108/0166 →
CHANGE OF NAME Recorded Jun 16, 2014
From: DOW GLOBAL TECHNOLOGIES INC.
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 033181/0810 →
Continuity (4)
Continuation 13867171 · Apr 22, 2013
Continuation 12067832
Provisional Application 60796809 · May 2, 2006
Related Publication 20140256883A1 · Sep 11, 2014