Ethylene polymerization process
View Patent ↗A process for polymerizing ethylene is disclosed. The polymerization is performed in the presence of a Ziegler-Natta catalyst system in two slurry reaction zones. Most of the polyethylene (70-95 wt. %) is produced in one of the zones, while a smaller fraction is produced in the other zone. The ratio of the weight average molecular weight of the smaller fraction to that of the larger fraction is greater than 8:1. The resulting polyethylene blend, which should have both high melt strength and high extrudate swell, will be useful for blow-molding applications.
1. A process which comprises polymerizing ethylene in the presence of a Ziegler-Natta catalyst system in a reactor consisting of two slurry reaction zones, Zone A and Zone B, connected in series, wherein from 70-95% by weight of the polyethylene is produced in Zone A and the ratio of weight average molecular weight of Zone B: Zone A polyethylene is greater than 8:1, to produce a polyethylene blend with a bimodal molecular weight distribution, a density greater than 0.935 g/cm 3 , a ratio of Z-average molecular weight to weight average molecular weight (M z /M w ) of greater than 10, and an extrudate swell (So) at a melt strength expressed as the value of complex viscosity (ETA*) in megapoise at 190° and at a complex modulus of 2×10 4 dyn/cm 2 defined by:
So> 2.75−0.5·log 10 (ETA*).
2. The process of claim 1 wherein a C 3 -C 10 α-olefin is copolymerized with the ethylene.
3. The process of claim 1 wherein the ratio of the weight average molecular weights of Zone B: Zone A polyethylenes is from 20:1 to 50:1.
4. The process of claim 1 wherein the polyethylene blend has a density from 0.946 to 0.955 g/cm 3 .
5. The process of claim 1 wherein each zone is operated at a temperature of from about 60° to about 100° C.
6. The process of claim 1 wherein the polyethylene blend has an M z /M w greater than 15.
7. The process of claim 1 wherein the polyethylene blend has a long-chain-branching index less than 0.5.
8. The process of claim 1 wherein the Ziegler-Natta catalyst system comprises a cocatalyst selected from the group consisting of trialkylaluminums, dialkylaluminum halides and alkylaluminum dihalides, a Group 4-6 transition metal compound, and a magnesium compound.
9. The process of claim 8 wherein the Group 4-6 transition metal compound is a titanium compound.
10. The process of claim 8 wherein the Ziegler-Natta catalyst system comprises:
a) a cocatalyst selected from the group consisting of trialkylaluminums, dialkylaluminum halides, and alkylaluminum dihalides; and
b) a supported transition metal mixture comprising the reaction product of:
1) a halogen-containing Group 4-6 transition metal compound; and
2) an organoaluminum-siloxane containing mixture comprising the reaction product of:
(a) an organoaluminum compound; and
(b) the reaction product of a polymethyl-hydrosiloxane and an organic magnesium halide.
11. The process of claim 10 wherein the halogen-containing Group 4-6 transition metal compound is titanium tetrachloride.