Non-Coordinating Anion Type Activators Containing Cation Having Large Alkyl Groups
US-2019330139-A1 · Oct 31, 2019 · US
US11919981B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11919981-B2 |
| Application number | US-202117504978-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 19, 2021 |
| Priority date | Oct 22, 2020 |
| Publication date | Mar 5, 2024 |
| Grant date | Mar 5, 2024 |
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This invention relates to mono cyclopentadienyl pyridyl hydroxyl amine catalyst compounds represented by Formula I(a) or I(b):wherein: M is a group 3-12 metal; R1 is a hydrocarbyl group or a silyl group; R2, R3, R4, R5, R6, R7, R8, R9, and R10 are independently selected from the group consisting of hydrogen, hydrocarbyl, alkoxy, silyl, amino, aryloxy, halogen and phosphino, wherein any two adjacent R groups may be joined to form a saturated or unsaturated single or multicyclic hydrocarbyl ring or heterocyclic ring; and each X1 and X2 is independently an anionic leaving group or X1 and X2 may be joined together to form a dianionic group.
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What is claimed is: 1. A catalyst compound represented by Formula I(a) or I(b): wherein: M of Formula I(a) or I(b) is Ti, Zr, or Hf; R 1 is independently selected from the group consisting of a hydrocarbyl group and a silyl group; R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , and R 10 are independently selected from the group consisting of hydrogen, hydrocarbyl, alkoxy, silyl, amino, aryloxy, halogen and phosphino, wherein any two adjacent R groups may be joined to form a saturated or unsaturated hydrocarbyl ring or heterocyclic ring, wherein the ring has 5, 6, 7, or 8 ring atoms and wherein substitutions on the ring can join to form additional rings; and each X 1 and X 2 is independently an anionic leaving group and X 1 and X 2 may be joined together to form a dianionic group. 2. The catalyst compound of claim 1 , wherein R 1 of Formula I(a) or I(b) is selected from the group consisting of alkyl and aryl. 3. The catalyst compound of claim 2 , wherein R 1 of Formula I(a) or I(b) is cycloalkyl. 4. The catalyst compound of claim 1 , wherein R 1 of Formula I(a) or I(b) is selected from the group consisting of t-butyl, 3,5-dimethylphenyl, 2,3,4,5,6-pentamethylphenyl, and 2,4, 6-triisopropylphenyl. 5. The catalyst compound of claim 1 , wherein R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , and R 10 of Formula I(a) or I(b) are independently selected from the group consisting of hydrogen, alkyl, aryl, and alkoxy. 6. The catalyst compound of claim 1 , wherein R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , and R 10 of Formula I(a) or I(b) are independently selected from the group consisting of hydrogen, methyl, t-butyl, phenyl, 1-methylphenyl, t-butoxy, 3,5-dimethylphenyl, 2,3,4,5,6-pentamethylphenyl, and 2,4,6-triisopropylphenyl. 7. The catalyst compound of claim 1 , wherein the catalyst compound is a catalyst compound of Formula I(a) selected from the group consisting of: 8. The catalyst compound of claim 7 , wherein the catalyst compound of Formula I(a) is selected from the group consisting of: 9. The catalyst compound of claim 1 , wherein the catalyst compound is a catalyst compound of Formula I(b) selected from the group consisting of: 10. The catalyst compound of claim 7 , wherein the catalyst compound of Formula I(b) is selected from the group consisting of: 11. A process for the production of an ethylene alpha-olefin copolymer comprising: polymerizing ethylene and at least one C 3 -C 20 alpha-olefin by contacting the ethylene and the at least one C 3 -C 20 alpha-olefin with a catalyst system including the catalyst compound of claim 1 in at least one polymerization reactor at a reactor pressure of from 2 MPa to 200 MPa and a reactor temperature of from 10° C. to 250° C. to form an ethylene alpha-olefin copolymer. 12. The process of claim 11 , wherein the ethylene alpha-olefin copolymer has an Mw value of 1,000,000 g/mol or greater. 13. The process of claim 11 , wherein the ethylene alpha-olefin copolymer has an Mw value of from 1,000,000 g/mol to 8,000,000 g/mol. 14. The process of claim 11 , wherein the ethylene alpha-olefin copolymer has an Mw/Mn value of 4 or less. 15. The process of claim 14 , wherein the ethylene alpha-olefin copolymer has an Mw/Mn value of from 1 to 2. 16. The process of claim 14 , wherein the ethylene alpha-olefin copolymer has a comonomer content of from 1 wt % to 8 wt %. 17. A process for the production of an ethylene alpha-olefin copolymer comprising: polymerizing ethylene and at least one C 3 -C 20 alpha-olefin by introducing the ethylene and the at least one C 3 -C 20 alpha-olefin to a catalyst system in at least one polymerization reactor at a reactor pressure of from 2 MPa to 200 MPa and a reactor temperature of from 10° C. to 250° C. to form an ethylene alpha-olefin copolymer, wherein the catalyst system comprises: an activator; an optional support; and a catalyst compound represented by Formula I(a) or I(b): wherein: M of Formula I(a) or I(b) is Ti, Zr, or Hf; R 1 is independently selected from the group consisting of a hydrocarbyl group and a silyl group; R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , and R 10 are independently selected from the group consisting of hydrogen, hydrocarbyl, alkoxy, silyl, amino, aryloxy, halogen and phosphino, wherein any two adjacent R groups may be joined to form a saturated or unsaturated hydrocarbyl ring or heterocyclic ring, wherein the ring has 5, 6, 7, or 8 ring atoms and wherein substitutions on the ring can join to form additional rings; and each X 1 and X 2 is independently an anionic leaving group and X 1 and X 2 may be joined together to form a dianionic group. 18. The process of claim 17 , wherein R 1 of Formula I(a) or I(b) is selected from the group consisting of alkyl and aryl. 19. The process of claim 17 , wherein the catalyst compound is one or more of:
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Metallocenes · CPC title
NO · CPC title
Ethene · CPC title
Additive used together with the catalyst, excluding compounds containing Al or B · CPC title
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