Peroxide treated metallocene-based polyolefins with improved melt strength
US-9346897-B2 · May 24, 2016 · US
US9732197B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9732197-B2 |
| Application number | US-201615134464-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 21, 2016 |
| Priority date | May 14, 2013 |
| Publication date | Aug 15, 2017 |
| Grant date | Aug 15, 2017 |
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Disclosed herein are ethylene-based polymers having low densities and narrow molecular weight distributions, but high melt strengths for blown film processing. Such polymers can be produced by peroxide-treating a metallocene-catalyzed resin.
Opening claim text (preview).
The invention claimed is: 1. A process for preparing an ethylene polymer having a ratio of Mw/Mn of less than or equal to about 5, a ratio of Mz/Mw of less than or equal to about 2.3, and a zero-shear viscosity at 190° C. of greater than or equal to about 8×10 4 Pa-sec, the process comprising: contacting a base resin with a peroxide compound at a temperature in a range from about 120 to about 300° C. to generate peroxide groups at about 10-50 ppm of peroxide groups based on the weight of the base resin. 2. The process of claim 1 , wherein the step of contacting the base resin with the peroxide compound comprises melt processing a mixture of the base resin and the peroxide compound in a twin screw extrusion system. 3. The process of claim 2 , wherein the base resin is produced using a metallocene-based catalyst system. 4. the process of claim 1 , wherein the ethylene polymer has from about 0.008 to about 0.04 long chain branches (LCB) per 1000 total carbon atoms. 5. The process of claim 1 , wherein: the ratio of Mw/Mn is in a range from about 2 to about 5; the ratio of Mz/Mw is a range from about 1.5 to about 2.3; and the zero-shear viscosity at 190° C. is in a range from about 8×10 4 to about 2×10 6 Pa-sec. 6. The process of claim 5 , wherein the ethylene polymer is an ethylene/α-olefin copolymer. 7. The process of claim 6 , wherein the ethylene/α-olefin copolymer has: a peak melting point in a range from about 100 to about 120° C.; a difference between the peak melting point and the vicat softening temperature of less than or equal to about 18° C.; a zero-shear viscosity at 190° C. in a range from about 1×10 5 to about 1×10 6 Pa-sec; and a CY-a parameter at 190° C. in a range from about 0.08 to about 0.28. 8. The process of claim 5 , wherein: the ethylene polymer is an ethylene/α-olefin copolymer characterized by a peak melting point in a range from about 100 to about 120° C., and a difference between the peak melting point and the vicat softening temperature of less than or equal to about 18° C.; and the base resin is characterized by a peak melting point in a range from about 100 to about 120° C., and a difference between the peak melting point and the vicat softening temperature of less than or equal to about 18° C. 9. The process of claim 5 , wherein: the ethylene polymer is an ethylene/α-olefin copolymer characterized by a zero-shear viscosity at 190° C. in a range from about 1×10 5 to about 1×10 6 Pa-sec, and a CY-a parameter at 190° C. in a range from about 0.08 to about 0.28; and the base resin is characterized by a zero-shear viscosity at 190° C. in a range from about 2×10 3 to about 7×10 4 Pa-sec, and a CY-a parameter at 190° C. in a range from about 0.4 to about 0.8. 10. The process of claim 5 , wherein: the ethylene polymer has from about 0.009 to about 0.035 long chain branches (LCB) per 1000 total carbon atoms; and the base resin has less than about 0.005 long chain branches (LCB) per 1000 total carbon atoms. 11. The process of claim 1 , wherein the ethylene polymer has: a ratio of Mw/Mn in a range from about 2.1 to about 3.5; a ratio of Mz/Mw in a range from about 1.5 to about 2.2; a melt index in a range from 0 to about 1; and a zero-shear viscosity at 190° C. in a range from about 1×10 5 to about 1×10 6 Pa-sec. 12. The process of claim 11 , wherein the ethylene polymer has a CY-a parameter at 190° C. in a range from about 0.1 to about 0.2. 13. The process of claim 11 , wherein the ethylene polymer has from about 0.01 to about 0.03 long chain branches (LCB) per 1000 total carbon atoms. 14. The process of claim 11 , wherein the ethylene polymer has a peak melting point in a range from about 105 to about 120° C. 15. The process of claim 11 , wherein the ethylene polymer is an ethylene/α-olefin copolymer with a density in a range from about 0.91 to about 0.92 g/cm 3 . 16. The process of claim 15 , wherein the ethylene/α-olefin copolymer is an ethylene/1-hexene copolymer. 17. The process of claim 11 , wherein the base resin has: a ratio of Mw/Mn in a range from about 2 to about 3.5; a ratio of Mz/Mw in a range from about 1.5 to about 2.2; and a melt index in a range from about 0.5 to about 2. 18. The process of claim 17 , wherein the base resin has: a zero-shear viscosity at 190° C. in a range from about 3×10 3 to about 2×10 4 Pa-sec; a CY-a parameter at 190° C. in a range from about 0.5 to about 0.8; and less than about 0.005 long chain branches (LCB) per 1000 total carbon atoms. 19. The process of claim 1 , wherein the ethylene polymer is an ethylene/1-hexene copolymer characterized by: a ratio of Mw/Mn in a range from about 2 to about 3.5; a ratio of Mz/Mw in a range from about 1.5 to about 2.2; and a density in a range from about 0.905 to about 0.925 g/cm 3 . 20. The process of claim 19 , wherein the ethylene/1-hexene copolymer has: a zero-shear viscosity at 190° C. in a range from about 1×10 5 to about 1×10 6 Pa-sec; a CY-a parameter at 190° C. in a range from about 0.08 to about 0.28; and from about 0.008 to about 0.04 long chain branches (LCB) per 1000 total carbon atoms.
Polyethene · CPC title
characterised by the choice of material · CPC title
having particular viscosity · CPC title
including a reactive processing step which leads, inter alia, to morphological and/or rheological modifications, e.g. visbreaking · CPC title
Manufacture of films or sheets · CPC title
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