Bimodal polyethylene resins
A high density, high polydispersity polyethylene having improved properties, and a process of producing same.
1. An ethylene-based polymer comprising a higher molecular weight component (HMW component) and a lower molecular weight component (LMW component), the ethylene-based polymer being characterized by a density greater than or equal to 0.949 g/cm 3 , measured according to ASTM D792, a ratio of Mw/Mn of from 25 to 35, an Environmental Stress Crack Resistance (ESCR) of at least 600 hr. measured according to ASTM D-1693, Condition B octylphenoxypolyethoxyethanol 10%, and by a bimodal weight average molecular weight distribution with a local minimum in a range of log (molecular weight) 4 to 6 between a peak representing the HMW component and a peak representing the LMW component, as determined by Gel Permeation Chromatography (GPC) analysis, of the ethylene-based polymer, wherein the Mz/Mw of the high molecular weight component is from 3.3 to 5.
2. The ethylene-based polymer of claim 1 wherein the ethylene-based polymer has a split, and the split of the ethylene-based polymer is from 20 wt % to 45 wt %.
3. The ethylene-based polymer of claim 1 wherein the ethylene-based polymer is a polyethylene resin and has an ESCR of at least 650 hr measured according to ASTM D-1693 at F50.
4. The ethylene-based polymer of claim 1 wherein the ethylene-based polymer has a melt flow ratio I21/I5 in the range from 15 to 45 measured according to ASTM D1238 with I21 and I5 measured at 190° C. and 21.6 kg or 5.0 kg weight respectively, and a flow index I21 in the range from 15 to 61 g/10 min.
5. The ethylene-based polymer of claim 1 wherein the ethylene-based polymer has a Capillary Swell t1000 of at least 6 seconds as measured by the extrudate covering a distance of 23 cm when extruded at a shear rate of 1000 1/s, with a 12 mm diameter barrel and a 1 mm diameter circular die of length 10 mm, with a 90° C. entrance angle.
6. A process for copolymerizing ethylene and one or more alpha-olefins in a single olefin polymerization reactor utilizing a catalyst system, an activator and a support in order to produce an ethylene-based polymer, the process comprising combining ethylene and at least one alpha-olefin comonomer in the presence of a catalyst system, an activator and a support, wherein the catalyst system comprises a main catalyst and a trim catalyst, wherein the main catalyst comprises bis(2-pentamethylphenylamido)ethyl)zirconium dibenzyl, and wherein the trim catalyst comprises at least one of (propylcyclopentadienyl)(1,3-dimethyl-tetrahydroindenyl)zirconium dimethyl and (methylcyclopentadienyl)(1-methyl-tetrahydroindenyl)zirconium dimethyl, wherein the ethylene-based polymer that is produced is an ethylene-based polymer having a higher molecular weight component (HMW component) and a lower molecular weight component (LMW component) and a bimodal molecular weight distribution, the ethylene-based polymer being characterized by a density greater than or equal to 0.949 g/cm 3 , measured according to ASTM D792, a ratio of Mw/Mn of from 25 to 35, an ESCR of at least 600 hr. measured according to ASTM D-1693 at F50, Condition B octylphenoxypolyethoxyethanol 10%, and by a bimodal weight average molecular weight distribution with a local minimum in a range of log (molecular weight) 4 to 6 between a peak representing the maximum of the HMW component and a peak representing the maximum of the LMW component, as determined by Gel Permeation Chromatography (GPC) analysis, of the ethylene-based polymer, and wherein the Mz/Mw of the high molecular weight component is from 3.3 to 5.
7. An article manufactured using the ethylene-based polymer of claim 1 .
8. The article of claim 7 wherein the article is prepared by blow molding.