Processes for producing fluorided solid oxides and uses thereof in metallocene-based catalyst systems

US11731122B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11731122-B2
Application numberUS-202217855874-A
CountryUS
Kind codeB2
Filing dateJul 1, 2022
Priority dateSep 27, 2018
Publication dateAug 22, 2023
Grant dateAug 22, 2023

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

Official abstract text for this publication.

Disclosed herein are methods for preparing fluorided solid oxides by contacting an acidic fluorine-containing compound with an inorganic base to form an aqueous mixture having a pH of at least 4, followed by contacting a solid oxide with the aqueous mixture to produce the fluorided solid oxide. Also disclosed are methods for preparing fluorided solid oxides by contacting an acidic fluorine-containing compound with a solid oxide to produce a mixture, followed by contacting the mixture with a inorganic base to produce the fluorided solid oxide at a pH of at least about 4. The fluorided solid oxide can be used as an activator component in a catalyst system for the polymerization of olefins.

First claim

Opening claim text (preview).

We claim: 1. A fluorided solid oxide comprising: a silica-coated alumina; from about 0.5 to about 15 wt. % F; and from about 0.5 to about 15 wt. % Zn; wherein the fluorided solid oxide comprises ZnSiF 6 . 2. A catalyst composition comprising a metallocene compound, the fluorided solid oxide of claim 1 , and an optional co-catalyst. 3. The composition of claim 2 , wherein a catalyst activity of the catalyst composition is greater than about 6000 grams of polyethylene per gram of the fluorided solid oxide per hour, under slurry polymerization conditions, with a triisobutylaluminum co-catalyst, using isobutane as a diluent, and with a polymerization temperature of 95° C. and a reactor pressure of 400 psig. 4. An olefin polymerization process, the process comprising: contacting the catalyst composition of claim 2 with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization conditions to produce an olefin polymer. 5. The fluorided solid oxide of claim 1 , wherein the fluorided solid oxide comprises from about 2 to about 9 wt. % F, and from about 0.5 to about 5 wt. % Zn. 6. The fluorided solid oxide of claim 1 , wherein the fluorided solid oxide further comprises from about 0.3 to about 1 wt. % B. 7. The fluorided solid oxide of claim 1 , wherein the fluorided solid oxide has: a total pore volume from about 0.5 to about 2.5 mL/g; a BET surface area from about 150 to about 700 m 2 /g; and an average (d50) particle size from about 20 to about 100 microns. 8. The fluorided solid oxide of claim 1 , wherein: the silica-coated alumina contains from about 25 to about 50 wt. % silica, based on the weight of the silica-coated alumina. 9. The fluorided solid oxide of claim 1 , wherein the fluorided solid oxide comprises from about 3 to about 7 wt. % F, and from about 1 to about 5 wt. % Zn. 10. The fluorided solid oxide of claim 9 , wherein the fluorided solid oxide has: a total pore volume from about 0.5 to about 2.5 mL/g; a BET surface area from about 150 to about 700 m 2 /g; and an average (d50) particle size from about 20 to about 100 microns. 11. The fluorided solid oxide of claim 10 , wherein the silica-coated alumina contains from about 25 to about 50 wt. % silica, based on the weight of the silica-coated alumina. 12. The fluorided solid oxide of claim 1 , wherein the fluorided solid oxide comprises from about 4 to about 10 wt. % ZnSiF 6 . 13. A fluorided solid oxide comprising: a silica-coated alumina; from about 0.5 to about 15 wt. % F; from about 0.5 to about 15 wt. % Zn; and from about 0.2 to about 1.2 wt. % B. 14. The fluorided solid oxide of claim 13 , wherein the fluorided solid oxide comprises: from about 2 to about 9 wt. % F; and from about 0.5 to about 5 wt. % Zn. 15. The fluorided solid oxide of claim 13 , wherein the fluorided solid oxide has: a total pore volume from about 0.5 to about 2.5 mL/g; a BET surface area from about 150 to about 700 m 2 /g; and an average (d50) particle size from about 20 to about 100 microns. 16. The fluorided solid oxide of claim 13 , wherein the fluorided solid oxide comprises Zn(BF 4 ) 2 . 17. The fluorided solid oxide of claim 13 , wherein: the silica-coated alumina contains from about 25 to about 50 wt. % silica, based on the weight of the silica-coated alumina. 18. A catalyst composition comprising a metallocene compound, the fluorided solid oxide of claim 13 , and an optional co-catalyst. 19. The composition of claim 18 , wherein a catalyst activity of the catalyst composition is greater than about 6000 grams of polyethylene per gram of the fluorided solid oxide per hour, under slurry polymerization conditions, with a triisobutylaluminum co-catalyst, using isobutane as a diluent, and with a polymerization temperature of 95° C. and a reactor pressure of 400 psig. 20. An olefin polymerization process, the process comprising: contacting the catalyst composition of claim 18 with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization conditions to produce an olefin polymer. 21. The fluorided solid oxide of claim 13 , wherein the fluorided solid oxide comprises: from about 3 to about 7 wt. % F; from about 1 to about 5 wt. % Zn; and from about 0.3 to about 1 wt. % B. 22. The fluorided solid oxide of claim 21 , wherein the fluorided solid oxide has: a total pore volume from about 0.5 to about 2.5 mL/g; a BET surface area from about 150 to about 700 m 2 /g; and an average (d50) particle size from about 20 to about 100 microns. 23. The fluorided solid oxide of claim 22 , wherein the silica-coated alumina contains from about 25 to about 50 wt. % silica, based on the weight of the silica-coated alumina. 24. The fluorided solid oxide of claim 13 , wherein the fluorided solid oxide comprises from about 4 to about 10 wt. % Zn(BF 4 ) 2 . 25. The fluorided solid oxide of claim 13 , wherein: the silica-coated alumina contains from about 25 to about 50 wt. % silica, based on the weight of the silica-coated alumina; and the fluorided solid oxide comprises Zn(BF 4 ) 2 . 26. A fluorided solid oxide comprising: a silica-coated alumina; and Zn(BF 4 ) 2 , ZnSiF 6 , or a combination thereof.

Assignees

Inventors

Classifications

  • Features related to the catalyst preparation, the catalyst use or to the deactivation of the catalyst · CPC title

  • Compounds containing silicon, fluorine, and other elements · CPC title

  • After-treatment of oxides or hydroxides · CPC title

  • Ethene · CPC title

  • supported on a carrier, e.g. silica, MgCl2, polymer · CPC title

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What does patent US11731122B2 cover?
Disclosed herein are methods for preparing fluorided solid oxides by contacting an acidic fluorine-containing compound with an inorganic base to form an aqueous mixture having a pH of at least 4, followed by contacting a solid oxide with the aqueous mixture to produce the fluorided solid oxide. Also disclosed are methods for preparing fluorided solid oxides by contacting an acidic fluorine-cont…
Who is the assignee on this patent?
Chevron Phillips Chemical Co Lp
What technology area does this patent fall under?
Primary CPC classification C08F4/65916. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Aug 22 2023 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 7 related publications on this page (citations in our corpus or others sharing the same primary CPC).