IP Library Granted Patent US 7,678,868
Granted Patent B2
US 7,678,868 · App. 12/352,173 · Granted Mar 16, 2010

Self limiting catalyst composition and propylene polymerization process

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Quick Facts
Patent No.
US 7,678,868
App. No.
12/352,173
Granted
Mar 16, 2010
Kind
B2
Abstract

A catalyst composition for the polymerization of propylene comprising one or more Ziegler-Natta procatalyst compositions comprising one or more transition metal compounds and one or more esters of aromatic dicarboxylic acid internal electron donors; one or more aluminum containing cocatalysts; a selectivity control agent (SCA) comprising at least one silicon containing compound containing at least one C 1-10 alkoxy group bonded to a silicon atom, and one or more activity limiting agent (ALA) compounds comprising one or more aliphatic or cycloaliphatic carboxylic acids; alkyl-, cycloalkyl- or alkyl(poly)(oxyalkyl)-(poly)ester derivatives thereof; or inertly substituted derivatives of the foregoing.

Claims (28)

1. A polymerization process comprising:

charging an effluent of a first polymerization reactor to a second polymerization reactor;

contacting the effluent with propylene and a copolymerizable comonomer under polymerization conditions in the second polymerization reactor;

adding a mixture of a selectivity control agent (SCA) comprising one or more silicon containing compounds and an activity limiting agent (ALA) selected from the group consisting of a C 1-20 alkyl ester of an aliphatic C 8-20 monocarboxylic acid, a C 2-20 alkyl mono- or poly-carboxylate derivative of a C 2-100 polyglycol, and combinations thereof to the second polymerization reactor; and

forming a copolymer.

2. The polymerization process of claim 1 wherein the effluent comprises a polypropylene and the copolymerizable copolymer is ethylene, the process comprising forming a copolymer of propylene and ethylene in the presence of the polypropylene in the second reactor.

3. The process of claim 1 comprising adding the SCA/ALA mixture to the second reactor and eliminating fouling in the second reactor.

4. The polymerization process of claim 1 comprising mixing the ALA with the SCA before the adding.

5. The process of claim 1 comprising forming the SCA/ALA mixture in the second reactor in situ.

6. The process of claim 1 comprising imparting no undesired odor to the copolymer.

7. A polymerization process comprising:

preparing a polypropylene in a first polymerization reactor;

preparing a copolymer of ethylene and propylene in the presence of the polypropylene in a second polymerization reactor; and

adding, to at least one of the polymerization reactors, a mixture of a selectivity control agent (SCA) comprising one or more silicon containing compounds and an activity limiting agent (ALA) selected from the group consisting of a C 1-20 alkyl ester of an aliphatic C 8-20 monocarboxylic acid, a C 2-20 alkyl mono- or poly-carboxylate derivative of a C 2-100 polyglycol, and combinations thereof.

8. The process of claim 7 comprising adding the SCA/ALA mixture to a member selected from the group consisting of the first polymerization reactor, the second polymerization reactor, and combinations thereof.

9. The process of claim 7 comprising adding the SCA/ALA mixture to the second polymerization reactor.

10. The process of claim 7 comprising adding a first SCA/ALA mixture to the first polymerization reactor and adding a second SCA/ALA mixture to the second reactor.

11. The process of claim 7 comprising forming, in the second polymerization reactor, a copolymer comprising the polypropylene and the copolymer of ethylene and propylene.

12. The polymerization process of claim 7 comprising adding a mixture comprising the SCA and an ALA selected from the group consisting of a C 1-20 alkyl ester of an aliphatic C 8-20 monocarboxylic acid, a C 2-20 alkyl mono- or poly-carboxylate derivative of a C 2-100 polyglycol, and combinations thereof.

13. The process of claim 7 comprising adding the SCA/ALA mixture to the second polymerization reactor; and eliminating fouling in the second polymerization reactor.

14. A polymerization process comprising:

preparing a copolymer of ethylene and propylene in the presence of a polypropylene in a polymerization reactor under polymerization conditions; and

adding, to the polymerization reactor, a mixture of a selectivity control agent (SCA) comprising one or more silicon containing compounds and an activity limiting agent (ALA) selected from the group consisting of a C 1-20 alkyl ester of an aliphatic C 8-20 monocarboxylic acid, a C 2-20 alkyl mono- or poly-carboxylate derivative of a C 2-100 polyglycol, and combinations thereof.

15. The polymerization process of claim 14 comprising adding a mixture comprising the SCA and an ALA selected from the group consisting of a C 1-20 alkyl ester of an aliphatic C 8-20 monocarboxylic acid, a C 2-20 alkyl mono- or poly-carboxylate derivative of a C 2-100 polyglycol, and combinations thereof.

16. The polymerization process of claim 14 comprising eliminating, with the addition of the SCA/ALA mixture, fouling in the polymerization reactor.

17. The polymerization process of claim 14 comprising separately adding the ALA and separately adding the SCA to the polymerization reactor.

18. The polymerization process of claim 14 comprising mixing the ALA and the SCA before the adding.

19. The polymerization process of claim 14 comprising preparing the polypropylene in a first polymerization reactor and preparing the copolymer of ethylene and propylene in a second polymerization reactor.

Assignments (9)
SECURITY INTEREST Recorded Apr 2, 2023
From: W. R. GRACE & CO.-CONN.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION
Reel/Frame 063199/0472 →
RELEASE OF SECURITY INTEREST Recorded Sep 23, 2021
From: GOLDMAN SACHS BANK USA
To: W. R. GRACE & CO.-CONN.
Reel/Frame 057594/0026 →
TERM LOAN SECURITY AGREEMENT Recorded Sep 23, 2021
From: W. R. GRACE & CO.-CONN.
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 057594/0104 →
NOTES SECURITY AGREEMENT Recorded Sep 23, 2021
From: W. R. GRACE & CO.-CONN.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION
Reel/Frame 057594/0156 →
SECURITY INTEREST Recorded Apr 3, 2018
From: W. R. GRACE & CO.-CONN.
To: GOLDMAN SACHS BANK USA, AS COLLATERAL AGENT
Reel/Frame 045828/0683 →
RELEASE OF SECURITY AGREEMENT RECORDED AT REEL/FRAME NO.: 032159/0384 Recorded Apr 3, 2018
From: GOLDMAN SACHS BANK USA, AS THE COLLATERAL AGENT
To: W.R. GRACE & CO.-CONN.
Reel/Frame 045832/0887 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE NAME TO "W. R. GRACE & CO. - CONN." PREVIOUSLY RECORDED ON REEL 032554 FRAME 0730. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNEE NAME WAS PREVIOUSLY INCORRECTLY LISTED IN THE RECORDATION COVER SHEET DATED 3/28/2014 AS "W. R. GRACE & CO. CONN.". Recorded Apr 2, 2014
From: DOW GLOBAL TECHNOLOGIES LLC; UNION CARBIDE CHEMICALS & PLASTICS TECHNOLOGY LLC
To: W. R. GRACE & CO. - CONN.
Reel/Frame 032589/0554 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 28, 2014
From: DOW GLOBAL TECHNOLOGIES LLC; UNION CARBIDE CHEMICALS & PLASTICS TECHNOLOGY LLC
To: W. R. GRACE & CO. CONN.
Reel/Frame 032554/0730 →
SECURITY AGREEMENT Recorded Feb 4, 2014
From: W.R. GRACE & CO.-CONN.
To: GOLDMAN SACHS BANK USA, AS THE COLLATERAL AGENT
Reel/Frame 032159/0384 →