IP Library Granted Patent US 7,091,291
Granted Patent B1
US 7,091,291 · App. 11/286,496 · Granted Aug 15, 2006

Olefin polymerization process

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,091,291
App. No.
11/286,496
Granted
Aug 15, 2006
Kind
B1
Abstract

A process for polymerizing an alpha-olefin is disclosed. The polymerization is performed in the presence of a catalyst system comprising a three-membered titanacycle. A wide variety of titanacycles can be readily prepared, making this a versatile and inexpensive olefin polymerization process.

Claims (22)

1. A process which comprises polymerizing an alpha-olefin in the presence of a catalyst system comprising a three-membered titanacycle wherein the two remaining atoms forming the titanacycle are selected from the group consisting of: oxygen in combination with carbon, sulfur, or phosphorus; monosubstituted nitrogen in combination with oxygen or carbon; and unsubstituted nitrogen in combination with carbon.

2. The process of claim 1 wherein the alpha-olefin is selected from the group consisting of ethylene, propylene, 1-butene, 1-hexene, 1-octene, and mixtures thereof.

3. The process of claim 1 wherein the catalyst system further comprises an aluminum compound selected from the group consisting of alkylaluminum halides, dialkylaluminum halides, and trialkylaluminums.

4. The process of claim 3 wherein the aluminum compound is a trialkylaluminum selected from the group consisting of triethylaluminum, triisobutylaluminum, and trimethylaluminum.

5. The process of claim 1 wherein the titanacycle has the general formula:

wherein R is selected from the group consisting of C 1 –C 20 hydrocarbyl and silyl; and each X is independently selected from the group consisting of halide, alkoxy, siloxy, alkylamino, and C 1 –C 30 hydrocarbyl.

6. The process of claim 1 wherein the titanacycle has the general formula:

wherein Q is selected from the group consisting of C, S, and P; each R is independently selected from the group consisting of C 1 –C 20 hydrocarbyl and silyl; when Q is C or S, n is 2; when Q is P, n is 3; and each X is independently selected from the group consisting of halide, alkoxy, siloxy, alkylamino, and C 1 –C 30 hydrocarbyl.

7. The process of claim 1 wherein the catalyst system further comprises a support.

8. The process of claim 7 wherein the support is selected from the group consisting of silica, alumina, magnesium chloride, and mixtures thereof.

9. The process of claim 7 wherein the support is magnesium chloride deposited on silica.

10. The process of claim 1 wherein the polymerization is performed at a temperature within the range of about 30° C. to about 100° C.

11. A slurry polymerization process of claim 1 .

12. A gas-phase polymerization process of claim 1 .

13. A process which comprises polymerizing an alpha-olefin in the presence of a catalyst system comprising a three-membered titanacycle having the general formula:

wherein Z is selected from the group consisting of oxygen, monosubstituted N, and disubstituted C; R is selected from the group consisting of C 1 –C 20 hydrocarbyl and silyl; and each X is independently selected from the group consisting of halide, alkoxy, siloxy, alkylamino, and C 1 –C 30 hydrocarbyl.

14. The process of claim 13 wherein the alpha-olefin is selected from the group consisting of ethylene, propylene, 1-butene, 1-hexene, 1-octene, and mixtures thereof.

15. The process of claim 13 wherein the catalyst system further comprises an aluminum compound selected from the group consisting of alkylaluminum halides, dialkylaluminum halides, and trialkylaluminums.

16. The process of claim 15 wherein the aluminum compound is a trialkylaluminum selected from the group consisting of triethylaluminum, triisobutylaluminum, and trimethylaluminum.

17. The process of claim 13 wherein the catalyst system further comprises a support.

18. The process of claim 17 wherein the support is selected from the group consisting of silica, alumina, magnesium chloride, and mixtures thereof.

19. The process of claim 13 wherein the polymerization is performed at a temperature within the range of about 30° C. to about 100° C.

Assignments (18)
RELEASE OF SECURITY INTEREST Recorded Jan 22, 2014
From: WELLS FARGO BANK, NATIONAL ASSOCIATION
To: EQUISTAR CHEMICALS, LP
Reel/Frame 032112/0786 →
APPOINTMENT OF SUCCESSOR ADMINISTRATIVE AGENT Recorded Jan 22, 2014
From: UBS AG, STAMFORD BRANCH
To: BANK OF AMERICA, N.A.
Reel/Frame 032112/0863 →
RELEASE OF SECURITY INTEREST Recorded Jan 22, 2014
From: CITIBANK, N.A.
To: EQUISTAR CHEMICALS, LP
Reel/Frame 032113/0644 →
RELEASE OF SECURITY INTEREST Recorded Jan 22, 2014
From: DEUTSCHE BANK TRUST COMPANY AMERICAS
To: EQUISTAR CHEMICALS, LP
Reel/Frame 032113/0684 →
RELEASE OF SECURITY INTEREST Recorded Jan 22, 2014
From: BANK OF AMERICA, N.A.
To: EQUISTAR CHEMICALS, LP
Reel/Frame 032113/0730 →
SECURITY AGREEMENT Recorded May 19, 2010
From: EQUISTAR CHEMICALS, LP
To: WELLS FARGO BANK, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 024402/0655 →
SECURITY AGREEMENT Recorded May 18, 2010
From: EQUISTAR CHEMICALS, LP
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 024397/0861 →
SECURITY AGREEMENT Recorded May 7, 2010
From: EQUISTAR CHEMICALS. LP
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 024351/0001 →
SECURITY AGREEMENT Recorded May 6, 2010
From: EQUISTAR CHEMICALS, LP
To: DEUTSCHE BANK TRUST COMPANY AMERICAS, AS COLLATERAL AGENT
Reel/Frame 024342/0443 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0705 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
To: EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0186 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0856 →
RELEASE OF SECURITY INTEREST Recorded May 4, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: EQUISTAR CHEMICALS, LP
Reel/Frame 024329/0535 →
SECURITY AGREEMENT Recorded Oct 30, 2009
From: EQUISTAR CHEMICALS, LP
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 023449/0687 →
SECURITY AGREEMENT Recorded Apr 9, 2009
From: EQUISTAR CHEMICALS, LP
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT AND COLLATERAL AGENT
Reel/Frame 022678/0860 →
SECURITY AGREEMENT Recorded Aug 4, 2008
From: BASELL POLYOLEFINE GMBH; ARCO CHEMICAL TECHNOLOGY L.P.; ARCO CHEMICAL TECHNOLOGY, INC.; ATLANTIC RICHFIELD COMPANY; BASELL NORTH AMERICA, INC.; BASELL POLYOLEFIN GMBH; LYONDELL CHEMICAL COMPANY; EQUISTAR CHEMICALS, L.P.
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 021354/0708 →
GRANT OF SECURITY INTEREST IN UNITED STATES PATENTS AND PATENT APPLICATIONS Recorded Mar 26, 2008
From: BASELL POLYOLEFINE GMBH; ARCO CHEMICAL TECHNOLOGY L.P.; ARCO CHEMICAL TECHNOLOGY, INC.; ATLANTIC RICHFIELD COMPANY; BASELL NORTH AMERICA, INC.; EQUISTAR CHEMICALS. LP.; LYONDELL CHEMICAL COMPANY; LYONDELL CHEMICAL TECHNOLOGY, L.P.; LYONDELL PETROCHEMICAL COMPANY; NATIONAL DISTILLERS AND CHEMICAL CORPORATION; OCCIDENTAL CHEMICAL CORPORATION; OLIN CORPORATION; QUANTUM CHEMICAL CORPORATION; BASELL POLYOLEFIN GMBH
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 020704/0562 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 17, 2006
From: NAGY, SANDOR
To: EQUISTAR CHEMICALS, LP
Reel/Frame 017469/0520 →