Catalyst activators, methods of preparation and use in polymerization processes
US-2017291973-A1 · Oct 12, 2017 · US
US11091567B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11091567-B2 |
| Application number | US-202016816507-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 12, 2020 |
| Priority date | Apr 15, 2019 |
| Publication date | Aug 17, 2021 |
| Grant date | Aug 17, 2021 |
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The present disclosure relates to amido-benzoquinone transition metal complexes, catalyst systems including amido-benzoquinone transition metal complexes, and polymerization processes to produce polyolefin polymers such as polyethylene-based polymers and polypropylene-based polymers.
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What is claimed is: 1. A catalyst system comprising a catalyst compound and an activator, wherein the catalyst compound is represented by Formula (I): wherein: M is a group 8, 9, or 10 transition metal; L is a Lewis base; j is 0, 1, or 2; X is an anionic ligand; k is 0, 1, or 2; and R 1 , R 2 , R 3 , and R 4 are independently selected from hydrogen, substituted or unsubstituted C 1 -C 30 hydrocarbyl, —CN, —NR′ 2 , —OR′, halogen, —NO 2 , —SiR′ 3 , five-, six-, or seven-membered heterocyclyl (where each R′ is independently hydrogen, C 1 -C 30 hydrocarbyl, and R′ is optionally substituted by halogen, or two R′ radicals optionally bond to form a five- or six-membered ring), or —SiR″ 3 , —SiR″ 2 (OR′″), —SiR″(OR′″) 2 , or —Si(OR′″) 3 (where each R″ and R′ is independently hydrogen, C 1 -C 30 hydrocarbyl, or two R″ radicals optionally bond to form a five- or six-membered ring); where R 1 , R 2 , R 3 , and R 4 are optionally substituted by halogen, —NO 2 , —CN, —CF 3 , —CF 2 CF 3 , —CH 2 CF 3 , —NR′ 2 , —OR′, —OSi(OR′) 3 , where each R′ is independently hydrogen, C 1 -C 30 hydrocarbyl, and R′ is optionally substituted by halogen, or two R′ radicals optionally bond to form a five- or six-membered ring, or —SiR″ 3 where each R″ is independently hydrogen, C 1 -C 30 hydrocarbyl, or two R″ radicals optionally bond to form a five- or six-membered ring; and the activator is represented by the Formula (II): wherein: M′ is selected from boron, aluminum, or gallium; E 1 , E 2 , and E 3 are oxygen; R a , R b , and R c are independently a C 1 -C 22 -alkyl, C 2 -C 22 -alkenyl, C 6 -C 22 -aryl, arylalkyl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 30 carbon atoms, alkylaryl where alkyl has from 1 to 10 carbon atoms and aryl has from 6 to 30 carbon atoms, a support material, or two or more of R a , R b , and R c are optionally bonded to form a five-, six- or seven-membered carbocyclic or heterocyclic ring, the heterocyclic ring being at least one atom selected from the group consisting of N, P, O and S; where R a , R b , and R c are optionally substituted by halogen, —NO 2 , —CF 3 , —CF 2 CF 3 , —CH 2 CF 3 , —NR′ 2 , —OR′(where each R′ is independently hydrogen, C 1 -C 22 -hydrocarbyl, and R′ is optionally substituted by halogen, or two R′ radicals optionally bond to form a five- or six-membered ring), or —SiR″ 3 (where each R″ is independently hydrogen, C 1 -C 22 -hydrocarbyl, or two R″ radicals optionally bond to form a five- or six-membered ring); w is 1; y is 1; and z is 1. 2. The catalyst system of claim 1 , wherein M is selected from Ni, Fe, or Co. 3. The catalyst system of claim 1 , wherein M is Ni. 4. The catalyst system of claim 1 , wherein X is selected from a halogen, alkoxy, methyl, ethyl, propyl, benzyl, phenyl, or naphthyl. 5. The catalyst system of claim 1 , wherein X is a phenyl. 6. The catalyst system of claim 1 , wherein L is an imine, an amine, a phosphine, a nitrile, an ether, a thioether, a sulfoxide, or a carbene. 7. The catalyst system of claim 1 , wherein L is a phosphine. 8. The catalyst system of claim 1 , wherein L is triphenylphosphine. 9. The catalyst system of claim 1 , wherein R 3 and R 4 together form an aryl. 10. The catalyst system of claim 1 , wherein R 1 is an aryl. 11. The catalyst system of claim 1 , wherein R 1 comprises a 2,6-substituted aryl. 12. The catalyst system of claim 11 , wherein the 2,6 substituted aryl is a 2,4,6-substituted aryl. 13. The catalyst system of claim 1 , wherein R 1 is 2,6-(diphenylmethyl)-4-methylphenyl. 14. The catalyst system of claim 1 , wherein R 2 is a hydrogen. 15. The catalyst system of claim 1 , wherein M′ is aluminum. 16. The catalyst system of claim 1 , wherein the catalyst represented by Formula (I) is one of the following: 17. The catalyst system of claim 1 , wherein the catalyst represented by Formula (I) is selected from: 18. The catalyst system of claim 1 , wherein the catalyst represented by Formula (I) is one of the following: 19. The catalyst system of claim 1 , wherein R a , R b , and R c have the same chemical structure. 20. The catalyst system of claim 1 , wherein R a , R b , and R c are perfluorophenyl. 21. The catalyst system of claim 1 , wherein at least one of R a , R b , or R c silica or alumina. 22. The catalyst system of claim 1 , further comprising a physical support material. 23. The catalyst system of claim 22 , wherein the physical support material is Al 2 O 3 , ZrO 2 , SiO 2 , TiO 2 , silica clay, silicon oxide/clay, or mixture(s) thereof. 24. A process for the production of an ethylene polymer comprising: polymerizing ethylene and optionally at least one C 3 -C 20 alpha-olefin by contacting the ethylene and the optional C 3 -C 20 alpha-olefin with the catalyst system of claim 1 in a gas phase reactor at a reactor pressure of from 0.7 to 70 bar and a reactor temperature of from 20° C. to 150° C. to form an ethylene polymer. 25. The process of claim 24 , wherein the catalyst has a productivity from 5,000 gPmmol −1 hr −1 to 100,000 gPmmol −1 hr −1 . 26. The process of claim 24 , wherein the catalyst has an activity from 50,000 gP/mmolCat/hour to 300,000 gP/mmolCat/hour. 27. The catalyst system of claim 1 , wherein the activator is one or more of
Ethene · CPC title
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