Catalyst systems for olefin polymerization
US-10526431-B2 · Jan 7, 2020 · US
US11111318B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11111318-B2 |
| Application number | US-201716317996-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 28, 2017 |
| Priority date | Jul 29, 2016 |
| Publication date | Sep 7, 2021 |
| Grant date | Sep 7, 2021 |
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Embodiments are directed to a metal complex formed, wherein the metal complexes are used as pro-catalyst in polyolefin polymerization and comprise the following structure (Formula (I)).
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The invention claimed is: 1. A polymerization process for producing an ethylene-based polymer comprising: polymerizing ethylene and at least one additional α-olefin in the presence of a catalyst system, wherein the catalyst system comprises a pro-catalyst defined by the metal ligand complex of formula (I): where: M is titanium, zirconium, or hafnium, each independently being in a formal oxidation state of +2, +3, or +4; and n is an integer of from 0 to 3, and wherein when n is 0, X is absent; and each X independently is a monodentate ligand that is neutral, monoanionic, or dianionic; or two Xs are taken together to form a bidentate ligand that is neutral, monoanionic, or dianionic; the metal ligand complex of formula (I) is, overall, neutral; each Z independently is O; R 1-7 and R 10-16 are selected from the group consisting of a (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, —Si(R C ) 3 , halogen atom, hydrogen atom, and combinations thereof; R 8 and R 9 are hydrogen atoms; R 23 and R 24 are —CH 2 —; R 17-22 are independently selected from a hydrogen atom and a (C 1 -C 40 )hydrocarbyl, wherein the sum of the non-hydrogen atoms for R 17-19 is larger than 1, and/or the sum of the non-hydrogen atoms for R 20-22 is larger than 1 and optionally two or more groups selected from R 17-22 can combine together to form a ring structure, with such ring structures having from 3 to 50 atoms in the ring, excluding any hydrogen atoms; at least one of R 1 and R 16 or both of R 1 and R 16 radicals selected from formula (II), formula (III), and formula (IV): R 31-35 , R 41-44 , and R 51-59 are independently chosen from a (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, —Si(R C ) 3 , halogen atom, hydrogen atom, and combinations thereof; and each R C is independently selected from (C 1 -C 30 )hydrocarbyl. 2. The polymerization process according claim 1 , wherein the catalyst system further comprises at least one cocatalyst. 3. The polymerization process according to claim 1 , wherein R 1 and R 16 are the same. 4. The polymerization process according to claim 1 , wherein (1) two of R 17-19 and two of R 20-22 are members in a C 5 -C 6 cycloalkyl ring structure or (2) two of R 17-19 or two of R 20-22 are members in a C 5 -C 6 cycloalkyl ring structure. 5. The polymerization process according to claim 1 , wherein at least one of R 1 and R 16 is formula (III) and at least one R 42 and R 43 is tert-butyl. 6. The polymerization process according to claim 1 , wherein at least one of R 1 and R 16 is formula (III) and R 41 and R 44 are hydrogen atoms. 7. The polymerization process according to claim 1 , wherein at least one of R 1 and R 16 is formula (IV). 8. The polymerization process according to claim 1 , wherein two of R 17-19 or two of R 20-22 are methyl groups. 9. The polymerization process according to claim 1 , wherein two of R 17-19 and two of R 20-22 are methyl groups. 10. The polymerization process according to claim 1 , wherein two of R 17-19 and two of R 20-22 are not hydrogen atoms.
Low density, i.e. < 0.91 g/cm3 · CPC title
Narrow molecular weight distribution, i.e. Mw/Mn < 3 · CPC title
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Polymerisation using regulators, e.g. chain terminating agents {, e.g. telomerisation} · CPC title
OOOO · CPC title
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