Bimodal polyethylene copolymers
Ethylene-based polymers are characterized by a density from 0.92 to 0.955 g/cm 3 , a HLMI of less than 35 g/10 min, and a ratio of a number of short chain branches (SCBs) per 1000 total carbon atoms at Mz to a number of SCBs per 1000 total carbon atoms at Mn in a range from 11.5 to 22. These polymers can have a higher molecular weight (HMW) component and a lower molecular weight (LMW) component, in which a ratio of a number of SCBs per 1000 total carbon atoms at Mn of the HMW component to a number of SCBs per 1000 total carbon atoms at Mn of the LMW component is in a range from 10.5 to 22. These ethylene polymers can be produced using a dual catalyst system containing an unbridged metallocene compound with an indenyl group having at least one halogen-substituted hydrocarbyl substituent with at least two halogen atoms, and a single atom bridged metallocene compound with a fluorenyl group and a cyclopentadienyl group.
1. An ethylene polymer having:
a density in a range from 0.92 to 0.955 g/cm 3 ;
a HLMI of less than or equal to 35 g/10 min; and
a ratio of a number of short chain branches (SCBs) per 1000 total carbon atoms at Mz to a number of SCBs per 1000 total carbon atoms at Mn in a range from 11.5 to 22.
2. An article comprising the ethylene polymer of claim 1 .
3. The article of claim 2 , wherein the ethylene polymer comprises an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, and/or an ethylene/1-octene copolymer.
4. The polymer of claim 1 , wherein:
the density is in a range from 0.92 to 0.95 g/cm 3 ;
the HLMI is less than or equal to 20 g/10 min; and
the ratio of the number of SCBs per 1000 total carbon atoms at Mz to the number of SCBs per 1000 total carbon atoms at Mn is in a range from 12 to 21.
5. The polymer of claim 4 , wherein the ethylene polymer has:
a molecular weight at D10 in a range from 750,000 to 2,000,000 g/mol;
a molecular weight at D85 in a range from 14,000 to 50,000; and
a number of SCBs per 1000 total carbon atoms at D10 in a range from 9 to 30.
6. The polymer of claim 4 , wherein the ethylene polymer has a number of SCBs per 1000 total carbon atoms at Mz in a range from 10 to 30.
7. The polymer of claim 1 , wherein:
the ethylene polymer has a bimodal molecular weight distribution; and
the ethylene polymer contains less than 0.1 ppm by weight, independently, of Mg, V, Ti, and Cr.
8. The polymer of claim 1 , wherein the ethylene polymer has:
a Mw in a range from 200,000 to 800,000 g/mol; and
a Mn in a range from 15,000 to 60,000 g/mol.
9. An article comprising the ethylene polymer of claim 8 , wherein the ratio of the number of SCBs per 1000 total carbon atoms at Mz to the number of SCBs per 1000 total carbon atoms at Mn is in a range from 13 to 19.
10. An ethylene polymer having:
a density in a range from 0.92 to 0.955 g/cm 3 ;
a HLMI of less than or equal to 35 g/10 min; and
a higher molecular weight component (HMW) and a lower molecular weight (LMW) component, wherein:
a ratio of a number of SCBs per 1000 total carbon atoms at Mn of the HMW component to a number of SCBs per 1000 total carbon atoms at Mn of the LMW component is in a range from 10.5 to 22.
11. An article comprising the ethylene polymer of claim 10 .
12. The polymer of claim 10 , wherein:
the density is in a range from 0.92 to 0.95 g/cm 3 ;
the HLMI is less than or equal to 20 g/10 min; and
the ratio of the number of SCBs per 1000 total carbon atoms at Mn of the HMW component to the number of SCBs per 1000 total carbon atoms at Mn of the LMW component is in a range from 11 to 21.
13. The polymer of claim 12 , wherein:
a ratio of a number of SCBs per 1000 total carbon atoms at Mp of the HMW component to a number of SCBs per 1000 total carbon atoms at Mp of the LMW component is in a range from 11 to 18; and
a ratio of a number of SCBs per 1000 total carbon atoms at Mp of the HMW component to a number of SCBs per 1000 total carbon atoms at Mz of the LMW component is in a range from 7.5 to 18.
14. The polymer of claim 10 , wherein:
a ratio of a number of SCBs per 1000 total carbon atoms at Mp of the HMW component to a number of SCBs per 1000 total carbon atoms at Mp of the LMW component is in a range from 11.5 to 16; and
ratio of a number of SCBs per 1000 total carbon atoms at Mp of the HMW component to a number of SCBs per 1000 total carbon atoms at Mz of the LMW component is in a range from 8 to 16.
15. The polymer of claim 14 , wherein the ethylene polymer comprises an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, and/or an ethylene/1-octene copolymer.
16. The polymer of claim 10 , wherein:
the HMW component has a Mn in a range from 400,000 to 800,000 g/mol; and
the LMW component has a Mz in a range from 70,000 to 200,000 g/mol.
17. The polymer of claim 16 , wherein an amount of the LMW component, based on the total polymer, is in a range of from 45 to 85 wt. %.
18. A polymerization process, the process comprising contacting a catalyst composition with ethylene and an α-olefin comonomer in a polymerization reactor system under polymerization conditions to produce an ethylene polymer, wherein the ethylene polymer has:
a density in a range from 0.92 to 0.955 g/cm 3 ;
a HLMI of less than or equal to 35 g/10 min; and
a ratio of a number of short chain branches (SCBs) per 1000 total carbon atoms at Mz to a number of SCBs per 1000 total carbon atoms at Mn in a range from 11.5 to 22; and
the catalyst composition comprises:
an unbridged metallocene compound containing two indenyl groups or an indenyl group and a cyclopentadienyl group, wherein at least one indenyl group has at least one halogen-substituted hydrocarbyl substituent with at least two halogen atoms;
a bridged metallocene compound with a cyclopentadienyl group and fluorenyl group, and an alkenyl substituent on the cyclopentadienyl group and/or on the bridging group;
an activator; and
optionally, a co-catalyst.
19. The process of claim 18 , wherein the activator comprises a fluorided solid oxide and/or a sulfated solid oxide.
20. The process of claim 18 , wherein the polymerization reactor system comprises a slurry reactor, gas-phase reactor, solution reactor, or a combination thereof.