Processes for preparing solid metallocene-based catalyst systems
US-9598515-B2 · Mar 21, 2017 · US
US10221258B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10221258-B2 |
| Application number | US-201715461523-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 17, 2017 |
| Priority date | Mar 17, 2017 |
| Publication date | Mar 5, 2019 |
| Grant date | Mar 5, 2019 |
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Methods for treating solid metallocene compounds that are exposed to air are disclosed. These methods include a step of contacting the exposed solid metallocene compound with a purging gas stream containing an inert gas, and optionally, subjecting the exposed solid metallocene compound to a sub-atmospheric pressure.
Opening claim text (preview).
We claim: 1. A method for treating an exposed solid metallocene compound, the method comprising, in any order: contacting the exposed solid metallocene compound with a purging gas stream comprising an inert gas; and subjecting the exposed solid metallocene compound to a sub-atmospheric pressure; to form a treated solid metallocene compound. 2. The method of claim 1 , wherein subjecting the exposed solid metallocene compound to a sub-atmospheric pressure comprises: a pressure in a range from about 100 torr to about 0.01 torr; and a temperature in a range from about 10° C. to about 75° C. 3. The method of claim 1 , wherein the method comprises at least two contacting steps and at least two subjecting steps, performed in any order. 4. The method of claim 1 , wherein a 1 mg/mL solution of the treated solid metallocene compound in toluene has a moisture content of less than 10 ppmw. 5. The method of claim 1 , wherein a color of a 1 mg/mL solution of the treated solid metallocene compound in toluene is unchanged for a time period of 24 hours at 25° C. 6. The method of claim 1 , wherein a catalyst activity of a 1 mg/mL solution of the treated solid metallocene compound in toluene is at least 85% of the catalyst activity obtained by using a 1 mg/mL solution of a fresh solid metallocene compound in toluene, after a time period of 24 hours at 25° C., under the same catalyst preparation and polymerization conditions. 7. A method for treating an exposed solid metallocene compound, the method comprising: contacting the exposed solid metallocene compound with a purging gas stream comprising an inert gas to form a treated solid metallocene compound. 8. The method of claim 7 , wherein: the inert gas comprises nitrogen; the purging gas stream comprises less than 25 ppmw of water; and the purging gas stream comprises less than 25 ppmw of oxygen-containing compounds. 9. The method of claim 7 , wherein the method does not comprise a recrystallization step. 10. The method of claim 7 , wherein the treated solid metallocene compound comprises an unbridged zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group. 11. The method of claim 7 , wherein: a 1 mg/mL solution of the treated solid metallocene compound in toluene has a moisture content of less than 5 ppmw; a color of a 1 mg/mL solution of the treated solid metallocene compound in toluene is unchanged for a time period of 36 hours at 25° C.; and a catalyst activity of a 1 mg/mL solution of the treated solid metallocene compound in toluene is at least 80% of the catalyst activity obtained by using a 1 mg/mL solution of a fresh solid metallocene compound in toluene, after a time period of 24 hours at 25° C., under the same catalyst preparation and polymerization conditions. 12. The method of claim 1 , wherein: the treated solid metallocene compound comprises titanium, zirconium, hafnium, or a combination thereof; and the method does not comprise a recrystallization step. 13. The method of claim 12 , wherein: subjecting the exposed solid metallocene compound to a sub-atmospheric pressure comprises a pressure of less than 10 torr; and a 1 mg/mL solution of the treated solid metallocene compound in toluene has a moisture content of less than 5 ppmw. 14. The method of claim 1 , wherein the treated solid metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group. 15. The method of claim 14 , wherein a catalyst activity of a 1 mg/mL solution of the treated solid metallocene compound in toluene is at least 80% of the catalyst activity obtained by using a 1 mg/mL solution of a fresh solid metallocene compound in toluene, after a time period of 24 hours at 25° C., under the same catalyst preparation and polymerization conditions. 16. The method of claim 1 , wherein the treated solid metallocene compound comprises an unbridged zirconium or hafnium based metallocene compound containing two cyclopentadienyl groups, two indenyl groups, or a cyclopentadienyl and an indenyl group. 17. The method of claim 16 , wherein: the purging gas stream is a nitrogen gas stream comprising less than 10 ppmw of water and less than 10 ppmw of oxygen-containing compounds; and a catalyst activity of a 1 mg/mL solution of the treated solid metallocene compound in toluene is at least 80% of the catalyst activity obtained by using a 1 mg/mL solution of a fresh solid metallocene compound in toluene, after a time period of 24 hours at 25° C., under the same catalyst preparation and polymerization conditions. 18. The method of claim 7 , wherein: the method comprises fluidizing the exposed solid metallocene compound with the purging gas stream; and the treated solid metallocene compound comprises titanium, zirconium, hafnium, or a combination thereof. 19. The method of claim 7 , wherein: the treated solid metallocene compound comprises a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group; and a catalyst activity of a 1 mg/mL solution of the treated solid metallocene compound in toluene is at least 85% of the catalyst activity obtained by using a 1 mg/mL solution of a fresh solid metallocene compound in toluene, after a time period of 24 hours at 25° C., under the same catalyst preparation and polymerization conditions. 20. The method of claim 7 , wherein the purging gas stream is a nitrogen gas stream comprising less than 10 ppmw of water and less than 10 ppmw of oxygen-containing compounds.
supported on a carrier, e.g. silica, MgCl2, polymer · CPC title
Cp or analog bridged to a non-Cp X neutral donor · CPC title
Ethene · CPC title
two cyclopentadienyl rings being mutually bridged · CPC title
two cyclopentadienyl rings being mutually non-bridged · CPC title
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