IP Library › Granted Patent US 11,168,161
Granted Patent B2
US 11,168,161 · App. 16/621,492 · Granted Nov 9, 2021

Biaryl phenoxy group IV transition metal catalysts for olefin polymerization

Inventors: Andrew M. Camelio (Midland, MI); Endre Szuromi (Lake Jackson, TX); David D. Devore (Midland, MI); Robert D. J. Froese (Midland, MI)
Assignee: Dow Global Technologies LLC
C08F210/16C07F7/28C08F4/64058C08F4/65908C08F4/65912C08F2420/05
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Quick Facts
Patent No.
US 11,168,161
App. No.
16/621,492
Granted
Nov 9, 2021
Kind
B2
Abstract

Embodiments are directed to catalyst systems comprising at least one metal ligand complex and to processes for polyolefin polymerization incorporating the catalyst systems. The metal ligand complexes have the following structures: (I)

Claims (37)

1. A catalyst system comprising a metal-ligand complex according to formula (I):

where

M is titanium, zirconium, or hafnium having a formal oxidation state of +2, +3, or +4;

each X is a monodentate or bidentate ligand independently selected from the group consisting of unsaturated (C 2 -C 50 )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 ;

n is 1, 2, or 3;

the metal-ligand complex has 6 or fewer metal-ligand bonds;

each Y is independently oxygen or sulfur;

each R 1 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;

Q is (C 2 -C 12 )alkylene, (C 2 -C 12 )heteroalkylene, (C 6 -C 50 )arylene, (C 4 -C 50 )heteroarylene, (—CH 2 Si(R C ) 2 CH 2 —), (—CH 2 CH 2 Si(R C ) 2 CH 2 CH 2 —), (—CH 2 Ge(R C ) 2 CH 2 —), or (—CH 2 CH 2 Ge(R C ) 2 CH 2 CH 2 —);

for each individual ring containing groups z 1 and z 2 , each of z 1 and z 2 is independently selected from the group consisting of sulfur, oxygen, —N(R R )—, ═N—, and —C(R R )—, provided that at least one of z 1 or z 2 is —C(R R )—;

each A is independently selected from the group consisting of -z 3 -z 4 -z 5 - and —C(R 3 )C(R 4 )C(R 5 )C(R 6 )—, where:

each of z 3 , z 4 , and z 5 is selected from the group consisting of sulfur, oxygen, —N(R R )—, and —C(R R )—, provided that exactly one of z 3 , z 4 , or z 5 is —C(R R )—or that exactly two of z 3 , z 4 , or z 5 are —C(R R )—; and

each R 3 , R 4 , R 5 , and R 6 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)—, 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;

each R C , R N , and R P in formula (I) is independently a (C 1 -C 50 )hydrocarbyl; and

each R R 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)—, 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 any two R R groups bonded to neighboring atoms are optionally linked.

2. The catalyst system according to claim 1 , wherein:

M is zirconium or hafnium;

each X is independently selected from the group consisting of (C 6 -C 20 )aryl, (C 4 -C 20 )heteroaryl, (C 4 -C 12 )diene, and a halogen;

each Y is oxygen; and

each R 1 is independently selected from the group consisting of (C 1 -C 50 )aryl and (C 4 -C 50 )heteroaryl.

3. The catalyst system according to claim 1 , wherein for each individual ring containing groups z 1 and z 2 , one of z 1 and z 2 is sulfur, and the other is —C(H) —.

4. The catalyst system according to claim 1 , wherein each A is —C(R 3 )C(R 4 )C(R 5 )C(R 6 )— each R 3 , R 4 , R 5 , and R 6 is —H.

5. The catalyst system according to claim 1 , wherein each R 1 is carbazolyl.

6. The catalyst system according to claim 1 , wherein each R 1 is phenyl or a substituted phenyl.

7. The catalyst system according to claim 1 , wherein R 1 is independently selected from the group consisting of carbazole; 3,6-di-tert-butylcarbazole; 3,6-bis-(2,4,6-trimethylphenyl)carbazole; 3,6-bis-(2,4,6-triisopropylphenyl)carbazole; 3,6-bis-(3,5-di-tert-butylphenyl)carbazole; 2,4,6-tri-iso-propylphenyl; 3,5-di-iso-propylphenyl; m-terphenyl; 3,5-bis-(2,4,6-trimethylphenyl)phenyl; 3,5-bis-(2,4,6-triisopropylphenyl)phenyl; and 3,5-bis-(3,5-di-tert-butylphenyl)phenyl groups.

8. The catalyst system according to claim 1 , wherein each R 1 is a substituted phenyl selected from the group consisting of 2,4,6-trimethylphenyl; 2,4,6-tri(iso-propyl)phenyl; 3,5-di-tert-butylphenyl, and 3,5-diphenylphenyl.

9. The catalyst system according to claim 1 , wherein each R 1 is independently 3,6-di-tert-butylcarbazol-9-yl or 2,7-di-tert-butylcarbazol-9-yl.

10. The catalyst system according to claim 1 , wherein each R 1 is 3,5-di-tert-butylphenyl.

11. The catalyst system according to claim 1 , wherein each R 1 is 2,4,6-trimethylphenyl.

12. The catalyst system according to claim 1 , where Q is (C 2 -C 12 )alkylene, (C 2 -C 12 )heteroalkylene, (C 6 -C 50 )arylene, (C 4 -C 50 )heteroarylene, (—CH 2 Si(R C ) 2 CH 2 —), (—CH 2 CH 2 Si(R C ) 2 CH 2 CH 2 —), (—CH 2 Ge(R C ) 2 CH 2 —), or (—CH 2 CH 2 Ge(R C ) 2 CH 2 CH 2 —).

13. The catalyst system according to claim 1 , wherein Q is chosen from —(CH 2 ) x —, where x is from 2 to 5.

14. The catalyst system according to claim 1 , wherein Q is —(CH 2 ) 4 —.

15. A polymerization process for producing an ethylene-based polymer, the polymerization process comprising:

polymerizing ethylene and at least one additional α-olefin in the presence of a catalyst system according to claim 1 and at least one activator to form a polymer.

16. A polymerization process for producing a propylene-based polymer, the polymerization process comprising:

polymerizing propylene and optionally one or more additional α-olefin in the presence of a catalyst system according to claim 1 and at least one activator to form a polymer.

17. The polymerization process according claim 16 , wherein the activator comprises MMAO, bis(hydrogenated tallow alkyl)methylammonium, tetrakis(pentafluorophenyl)borate, or tris(pentafluorophenyl)borane.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 11, 2019
From: CAMELIO, ANDREW M.; SZUROMI, ENDRE; DEVORE, DAVID D.; FROESE, ROBERT D.J.
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 051249/0574 →
Continuity (2)
Provisional Application 62522213 · Jun 20, 2017
Related Publication 20200157254A1 · May 21, 2020
Cited By (2)
US 12,221,508 US 12,297,311