Process for producing high molecular weight polyethylene

1. A process for producing polyethylene having a molecular weight of at least 3×10 5 g/mol as determined by ASTM 4020, the process comprising: contacting ethylene under polymerization conditions with a slurry of a catalyst composition in at least one hydrocarbon, wherein the catalyst composition comprises a Group 4 metal complex of a phenolate ether ligand and wherein the slurry includes from 5 to less than 40 ppm per liter of a compound effective to increase the conductivity of said at least one hydrocarbon.

2. The process of claim 1 wherein the slurry includes from 20 to 30 ppm per liter of said compound effective to increase the conductivity of said at least one hydrocarbon.

3. The process of claim 1 wherein said compound effective to increase the conductivity of said at least one hydrocarbon comprises at least one of a polysulfone copolymer, a polymeric polyamine, and an oil-soluble sulfonic acid.

4. The process of claim 1 wherein said at least one hydrocarbon comprises a C 8 to C 12 hydrocarbon.

5. The process of claim 1 wherein the Group 4 metal complex is disposed on a particulate support.

6. The process of claim 5 wherein the particulate support has an average particle size, d50, of less than 58 microns.

7. The process of claim 5 wherein the particulate support comprises an inorganic oxide.

8. The process of claim 1 wherein the Group 4 metal complex is a complex of a bis(phenolate) ether ligand.

9. The process of claim 1 wherein the Group 4 metal complex has the following general formula:

wherein at least two of the bonds from the oxygens (O) to M are covalent, with the other bonds being dative; AR is an aromatic group that can be the same or different from the other AR groups with each AR being independently selected from the group consisting of optionally substituted aryl and optionally substituted heteroaryl; B is a bridging group having from 3 to 50 atoms not counting hydrogen atoms and is selected from the group consisting of optionally substituted divalent hydrocarbyl and optionally substituted divalent heteroatom-containing hydrocarbyl; M is a metal selected from the group consisting of Hf and Zr; each L is independently a moiety that forms a covalent, dative or ionic bond with M; and n′ is 1, 2, 3 or 4.

10. The process of claim 8 wherein the bis(phenolate) ether ligand has the following general formula:

wherein each of R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 , and R 19 is independently selected from the group consisting of hydrogen, halogen, and optionally substituted hydrocarbyl, heteroatom-containing hydrocarbyl, alkoxy, aryloxy, silyl, boryl, phosphino, amino, alkylthio, arylthio, nitro, and combinations thereof; optionally two or more R groups can combine together into ring structures (for example, single ring or multiple ring structures), with such ring structures having from 3 to 12 atoms in the ring (not counting hydrogen atoms); and B is a bridging group having from 3 to 50 atoms not counting hydrogen atoms and is selected from the group consisting of optionally substituted divalent hydrocarbyl and optionally substituted divalent heteroatom-containing hydrocarbyl.

11. The process of any claim 8 wherein the bis(phenolate) ether ligand is selected from:

12. The process of claim 1 herein the Group 4 metal is zirconium.

13. The process of claim 5 wherein the particulate support has an average particle size, d50, of less than 50 microns.

14. The process of claim 5 wherein the particulate support has an average particle size, d50, of from 4 to 20 microns.

15. The process of claim 5 wherein the inorganic oxide is silica.