Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US12252573B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12252573-B2 |
| Application number | US-201917415365-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 20, 2019 |
| Priority date | Dec 21, 2018 |
| Publication date | Mar 18, 2025 |
| Grant date | Mar 18, 2025 |
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The polymerization process of this disclosure includes includes polymerizing ethylene and one or more olefins in the presence of a catalyst system under olefin polymerization conditions to form an ethylene-based polymer. The catalyst system comprising a metal-ligand complex according to formula (I).
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The invention claimed is: 1. A polymerization process comprising: polymerizing ethylene and one or more olefins in the presence of a catalyst system under olefin polymerization conditions to form an ethylene-based polymer, the catalyst system comprising a metal-ligand complex according to formula (I): where: M is a metal chosen from titanium, zirconium, or hafnium, the metal having a formal oxidation state of +2, +3, or +4; each X is a monodentate or bidentate ligand independently chosen from unsaturated (C 2 -C 20 )hydrocarbon, unsaturated (C 2 -C 50 )heterohydrocarbon, (C 1 -C 50 )hydrocarbyl, (C 6 -C 50 )aryl, (C 6 -C 50 )heteroaryl, cyclopentadienyl, substituted cyclopentadienyl, (C 4 -C 12 )diene, halogen, —N(R N ) 2 , and —NCOR C ; m is 1 or 2; n is 2 or 3; m+n=4; each A is independently chosen from —C(R 3a )C(R 4a )C(R 5a )C(R 6a )—, —C(R 3a )C(R 4a )C(R 5a )N—, —C(R 3a )C(R 4a )NC(R 6a )—, —C(R 3a )NC(R 5a )C(R 6a )—, —NC(R 4a )C(R 5a )C(R 6a )— or —NC(R 4a )NC(R 6a )—, in which optionally R 3a and R 4a , or R 4a and R 5a , or R 5a and R 6a are covalently connected to form an aromatic ring or a non-aromatic ring, or —C(R 3b )C(R 4b )G- or -GC(R 4c )C(R 5c )—, wherein G is N(R 3c ), N(R 5b ), O or S, and optionally R 3b and R 4b , or R 4c and R 5c are covalently connected to form an aromatic ring or a non-aromatic ring, and; each z 1 is independently selected from N or C(R 1 ); each z 2 is independently selected from N or C(R 2 ); each R 11 is anthracene-9-yl substituted with R S or more than one R S , wherein each R S is independently selected from (C 1 -C 12 )alkyl, (C 6 -C 15 )aryl, or (C 3 -C 12 )cycloalkyl; each R 1 , R 2 , R 3a , R 3b , R 3c , R 4a , R 4b , R 4c , R 5a , R 5b , R 5c , and R 6a is independently selected from the group consisting of (C 1 -C 50 ) hydrocarbyl, (C 1 -C 50 ) heterohydrocarbyl, (C 6 -C 50 ) aryl, (C 4 -C 50 ) heteroaryl, —Si(R C ) 3 , —Ge(R C ) 3 , —P(R P ) 2 , —N(R N ) 2 , —OR C , —SR C , —NO 2 , —CN, —CF 3 , R C S(O)—, —P(O)(R P ) 2 , R C S(O) 2 —, (R C ) 2 C═N—, R C C(O)O—, R C OC(O)—, R C C(O)N(R)—, (R C ) 2 NC(O)—, halogen, and —H, wherein each R N , R C , and R P is independently selected from the group consisting of (C 1 -C 20 )hydrocarbyl, (C 1 -C 20 )heterohydrocarbyl, and —H; when z 1 is C(R 1 ), R 1 and R 11 are not linked to form an aromatic ring or a non-aromatic ring: when z 2 is C(R 1 ) and z 2 is C(R 2 ), R 1 and R 2 are optionally linked to form an aromatic ring or a non-aromatic ring: provided that: when z 1 is CR 1 and z 2 is CR 2 , where R 1 and R 2 are not covalently connected to form an aromatic ring or a non-aromatic ring, m is 1 and n is 3. 2. The polymerization process of claim 1 , wherein A is —C(R 3a )C(R 4a )C(R 5a )C(R 6a )—, in which optionally R 3a and R 4a , or R 4a and R 5a , or R 5a and R 6a are covalently connected to form an aromatic ring or a non-aromatic ring, and the metal-ligand catalyst has a structure according to formula (II): where each z 1 , z 2 , R 11 , R 3a , R 4a , R 5a , R 6a , X, n, m, and M are defined as in formula (I). 3. The polymerization process of claim 1 , wherein A is -GC(R 4c )C(R 5c )— in which G is N(R 3c ), and optionally R 4c and R 5c are covalently connected to form an aromatic ring or a non-aromatic ring, and the metal-ligand catalyst has a structure according to formula (III): where each z 1 , z 2 , R 11 , R 3c , R 4c , R 5c , X, n, m, and M are defined as in formula (I). 4. The polymerization process of claim 1 , wherein A is —C(R 3b )C(R 4b )G- in which G is N(R 5b ), and optionally R 3b and R 4b are covalently connected to form an aromatic ring or a non-aromatic ring, and the metal-ligand catalyst has a structure according to formula (IV): where each z 1 , z 2 , R 11 , R 3b , R 4b , R 5b , X, n, m, and M are defined as in formula (I). 5. The polymerization process of claim 1 , wherein A is -GC(R 4c )C(R 5c )— in which G is S, and optionally R 4c and R 5c are covalently connected to form an aromatic ring or a non-aromatic ring, and the metal-ligand catalyst has a structure according to formula (V): where each z 1 , z 2 , R 11 , R 4c , R 5c , X, n, m, and M are defined as in formula (I). 6. The polymerization process of claim 1 , wherein m is 1. 7. The polymerization process of claim 1 , wherein z 1 is N. 8. The polymerization process of claim 1 , wherein X is benzyl, phenyl, or chloro. 9. The polymerization process of claim 1 , wherein R 11 is a radical of formula (VI): wherein R 12 , R 13 , R 14 , R 15 , and R 16 is chosen from (C 1 -C 10 )alkyl, (C 6 -C 10 )aryl, or —H. 10. The polymerization process of claim 9 , wherein R 12 , R 13 , R 14 , R 15 , and R 16 is chosen from tert-butyl, 3,5-di-tert-butylphenyl, or —H. 11. The polymerization process of claim 1 , wherein z 2 is N. 12. The polymerization process of claim 1 , wherein when z 2 is N and z 1 is CR 1 , R 1 and R 11 are not covalently connected to form an aromatic or non-aromatic ring. 13. The polymerization process of claim 1 , wherein the metal-ligand complex is selected from:
Compounds containing elements of Groups 4 or 14 of the Periodic Table · CPC title
condensed with carbocyclic rings or carbocyclic ring systems · CPC title
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
NN · CPC title
in combination with an ionising compound other than alumoxane, e.g. (C6F5)4B-X+ · CPC title
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