Bimodal linear low density polyethylene copolymer
Provided are bimodal linear low density polyethylene copolymers (B-LLDPE copolymers) that have a combination of improved properties comprising at least one processability characteristic similar or better than that of an unblended monomodal ZN-LLDPE and a dart impact property similar or better than that of an unblended monomodal MCN-LLDPE. For the various aspects, the B-LLDPE copolymer has a density from 0.8900 to 0.9300 g/cm 3 ; a melt index (I 2 ) from 0.1 g/10 min. to 5 g/10 min.; a M z from 600,000 to 1,900,000 g/mol; and a SHI from 5.35 to 75 η*(1.0)/η*(100). The B-LLDPE copolymer can be further characterized by a first melt flow ratio (I 21 /I 2 ) from 32 to 140 and a first molecular weight ratio (M z /M w ) from 4.5 to 11.
1 . A bimodal linear low density polyethylene copolymer comprising:
a density from 0.915 to 0.920 gram per cubic centimeter (g/cm 3 ) measured according to ASTM D792-13, Method B;
a melt index (I 2 ) from 3.2 grams per 10 minutes (g/10 min.) to 3.6 g/10 min., measured according to the Melt Index Test Method at 190° C. and 2.16 kilograms according to ASTM D1238-13;
a melt flow ratio (I 21 /I 2 ) from 60 to 140, measured according to the Melt Index Test Method at 190° C. and 21.6 and 2.16 kilograms, respectively, according to ASTM D1238-13;
a M z from 800,000 to 1,200,000 grams per mole (g/mol), measured according to a Gel Permeation Chromatography (GPC) Test Method; and
a shear thinning index (SHI) from 10 to 12 η*(1.0)/η*(100) measured according to SHI Test Method.
2 . The bimodal linear low density polyethylene copolymer of claim 1 having a first molecular weight ratio (M z /M w ) from 4 to 11, measured according to the GPC Test Method, wherein M z is z-average molecular weight and M w is weight-average molecular weight.
3 . The bimodal linear low density polyethylene copolymer of claim 1 ,
wherein the density is from 0.916 to 0.926 g/cm 3 measured according to ASTM D792-13, Method B.
4 . The bimodal linear low density polyethylene copolymer of claim 1 having a tan delta (tan δ) from 2 to 6, measured at 190° C. and a frequency of 0.1000 radians per second (rad/s) according to Tan Delta Test Method.
5 . The bimodal linear low density polyethylene copolymer of claim 4 , wherein the tan δ is from 5.6 to 6, measured at 190° C. and a frequency of 0.1000 radians per second (rad/s) according to Tan Delta Test Method;
the density is from 0.916 to 0.918 g/cm 3 measured according to ASTM D792-13, Method; and
the M z /M w is 5 to 5.6, measured according to the GPC Test Method.
6 . The bimodal linear low density polyethylene copolymer of claim 1 having a low elution fraction of 1.7 percent to 10 percent as measured by iCCD technique from above 25° C. to below 35° C.
7 . The bimodal linear low density polyethylene copolymer of claim 1 having a high density fraction of 0.9 percent to 4.1 percent as measured by iCCD technique from above 95° C. to below 115° C.
8 . The bimodal linear low density polyethylene copolymer of claim 1 having a tan delta (tan δ) from 3 to 4, measured at 190° C. and a frequency of 0.1000 radians per second (rad/s) according to Tan Delta Test Method.
9 . The bimodal linear low density polyethylene copolymer of claim 1 , having a tan delta (tan δ) from 1.6 to 3.1, measured at 190° C. and a frequency of 0.1000 radians per second (rad/s) according to Tan Delta Test Method.
10 . The bimodal linear low density polyethylene copolymer of claim 1 having a low elution fraction of 3.8 percent to 4.6 percent as measured by iCCD technique from above 25° C. to below 35° C.
11 . The bimodal linear low density polyethylene copolymer of claim 1 having a high density fraction of 6 percent to 10 percent as measured by iCCD technique from above 95° C. to below 115° C.
12 . A manufactured article comprising a shaped form of the bimodal linear low density polyethylene copolymer of claim 1 .
13 . A method of making the bimodal linear low density polyethylene copolymer of claim 1 , the method comprising contacting ethylene (“C 2 ”) and a comonomer (“C x ”) selected from 1-butene (C x =C 4 ), 1-hexene (C x =C 6 ), or both (C x =C 4 and C 6 ) at a comonomer-to-ethylene (C x /C 2 ) molar ratio of 0.005 to 0.30 with a bimodal catalyst system comprising bis[(2-pentamethylphenylamido)ethyl]amine zirconium dibenzyl in the presence of molecular hydrogen gas (H 2 ) at a hydrogen-to-ethylene (H 2 /C 2 ) molar ratio from 0.001 to less than 0.012, all in a single gas phase polymerization reactor containing a fluidized resin bed at a temperature from 70° C. to 90° C., thereby making the bimodal linear low density polyethylene copolymer.
14 . The method of claim 13 , wherein the H 2 /C 2 molar ratio is from 0.001 to 0.003.
15 . The method of claim 13 , wherein the bimodal catalyst system comprises a metallocene other than (tetramethylcyclopentadienyl) (n-propylcyclopentadienyl) zirconium-X 2 (X=chloride, methyl).