IP Library › Granted Patent US 7,906,614
Granted Patent B2
US 7,906,614 · App. 12/305,029 · Granted Mar 15, 2011

Polymer catalyst deactivation and acid neutralization using ionomers

Assignee: Dow Global Technologies LLC
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Quick Facts
Patent No.
US 7,906,614
App. No.
12/305,029
Granted
Mar 15, 2011
Kind
B2
Abstract

A process for deactivating an active catalyst species in an olefin polymer stream exiting a polymerization reactor and neutralizing catalyst residues comprising adding to the olefin polymer stream in a quantity at least sufficient to inactivate the catalyst species and neutralize catalyst residues a composition comprising an ionomer having a molecular weight of at least 100 g/mol, and subsequently recovering the resulting polymer product.

Claims (9)

1. A process for deactivating an active catalyst species in an olefin polymer stream exiting a polymerization reactor and neutralizing catalyst residues comprising adding to the olefin polymer stream in a quantity at least sufficient to inactivate the catalyst species and neutralize catalyst residues a composition comprising an ionomer having a molecular weight of at least 100 g/mol, and subsequently recovering the resulting polymer product, wherein the ionomer is a potassium hydroxide or sodium hydroxide partially or fully neutralized copolymer of ethylene with acrylic acid or methacrylic acid, said copolymer having a number average molecular weight from 500 g/mol to 5,000 g/mol.

2. A process for deactivating an active catalyst species in an olefin polymer stream exiting a polymerization reactor and concomitantly neutralizing catalyst residues comprising adding to the olefin polymer stream water or a hydroxyl group containing organic compound catalyst kill agent and an ionomer having a molecular weight of at least 100 g/mol, and subsequently recovering the resulting polymer product, wherein the ionomer is a potassium hydroxide or sodium hydroxide partially or fully neutralized copolymer of ethylene with acrylic acid or methacrylic acid, said copolymer having a number average molecular weight from 500 g/mol to 5,000 g/mol.

3. A process for deactivating an active catalyst species in an olefin polymer stream exiting a polymerization reactor and concomitantly neutralizing catalyst residues comprising adding to the olefin polymer stream a catalyst kill and acid neutralization composition consisting essentially of an ionomer having a molecular weight of at least 100 g/mol, and subsequently recovering the resulting polymer product, wherein the ionomer is a potassium hydroxide or sodium hydroxide partially or fully neutralized copolymer of ethylene with acrylic acid or methacrylic acid, said copolymer having a number average molecular weight from 500 g/mol to 5,000 g/mol.

4. A process according to any one of claims 1 - 3 wherein the ionomer is added to the olefin polymer stream prior to devolatilization of the polymer stream and the polymer product is recovered by devolatilization of the polymer stream.

5. The process according to any one of claims 1 - 3 wherein the olefin polymer is a homopolymer of ethylene or propylene or a copolymer of ethylene with one or more C 3-10 α-olefins prepared by use of a transition metal containing catalyst composition.

6. The process according to any one of claims 1 - 3 wherein the catalyst composition comprises halogen, a transition metal of Groups 3-6 of the Periodic Table of Elements, and optionally magnesium and/or an alkoxide; and an organoaluminum cocatalyst.

7. The process according to any one of claims 1 - 3 wherein from 0.01 to 10 percent of ionomer based on olefin polymer weight is employed.

8. The process according to claim 7 wherein the olefin polymer is a homopolymer of ethylene or propylene or a copolymer of ethylene with one or more C 3-10 α-olefins prepared by use of a transition metal containing catalyst composition.

9. The process according to claim 8 wherein the catalyst composition comprises halogen, a transition metal of Groups 3-6 of the Periodic Table of Elements, and optionally magnesium and/or an alkoxide; and an organoaluminum cocatalyst.

Assignments (4)
CHANGE OF NAME Recorded Mar 18, 2011
From: DOW GLOBAL TECHNOLOGIES INC.
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 025986/0407 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 9, 2011
From: VANSPEYBROECK, RONY S.L.
To: DOW BENELUX B.V.
Reel/Frame 025774/0244 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 9, 2011
From: DOW BENELUX B.V.
To: THE DOW CHEMICAL COMPANY
Reel/Frame 025774/0279 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 9, 2011
From: THE DOW CHEMICAL COMPANY
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 025774/0296 →
Continuity (2)
Provisional Application 60815132 · Jun 20, 2006
Related Publication 20090137754A1 · May 28, 2009