IP Library Granted Patent US 7,247,690
Granted Patent B2
US 7,247,690 · App. 10/818,429 · Granted Jul 24, 2007

Melt-fabricable tetrafluoroethylene/fluorinated vinyl ether copolymer prepared by suspension polymerization

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Quick Facts
Patent No.
US 7,247,690
App. No.
10/818,429
Granted
Jul 24, 2007
Kind
B2
Abstract

Melt-fabricable, tough copolymer of tetrafluoroethylene and fluorinated vinyl ether is produced in a suspension polymerization process by copolymerizing tetrafluoroethylene and fluorinated vinyl ether in a pressurized, agitated reaction vessel which contains aqueous medium, free radical initiator, and a telogen, the aqueous medium being essentially free of fluorine containing organic solvent. The contents of the reaction vessel are agitated during polymerization sufficiently to coagulate copolymer of tetrafluoroethylene and fluorinated vinyl ether. The melt-fabricable, tough copolymer having a melt viscosity of less than about 1×10 6 Pa·S is isolated directly from the reaction vessel.

Claims (26)

1. A process for producing a melt-fabricable, tough copolymer of tetrafluoroethylene and fluorinated vinyl ether in a suspension polymerization process comprising:

copolymerizing tetrafluoroethylene and fluorinated vinyl ether in a pressurized, agitated reaction vessel which contains aqueous medium, water-soluble free radical initiator, and a telogen, said aqueous medium being essentially free of fluorine containing organic solvent, said process employing fluorinated vinyl ether in an amount sufficient to produce melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether containing from about 1 to about 20 weight % fluorinated vinyl ether;

agitating the contents of said reaction vessel during said copolymerizing to coagulate copolymer of tetrafluoroethylene and fluorinated vinyl ether; and

isolating said melt-fabricable, tough copolymer having a melt viscosity of less than about 1×10 6 Pa·S directly from said reaction vessel.

2. The process of claim 1 wherein said process employs fluorinated vinyl ether in an amount sufficient to produce melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether containing from about 3 to about 20 weight % fluorinated vinyl ether.

3. The process of claim 1 wherein said process employs fluorinated vinyl ether in an amount sufficient to produce melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether containing from about 3 to about 15 weight % fluorinated vinyl ether.

4. The process of claim 1 wherein said process employs fluorinated vinyl ether in an amount sufficient to produce melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether containing from about 3 to about 10 weight % fluorinated vinyl ether.

5. The process of claim 1 further comprising employing a fluoroolefin comonomer in an amount sufficient to produce melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether containing up to 5 weight % of a fluoroolefin comonomer units.

6. The process of claim 5 wherein said fluoroolefin is hexafluoropropylene.

7. The process of claim 1 wherein said contents of said reaction vessel comprise less than 0.010 weight % surfactant based on the amount of water present.

8. The process of claim 1 wherein said telogen comprises a non-fluorine-containing organic compound.

9. The process of claim 1 wherein said telogen is an aliphatic hydrocarbon containing 1 to 6 carbon atoms.

10. The process of claim 1 wherein said melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether has a melt viscosity in the range of about 1×10 2 Pa·S to about 1×10 6 Pa·S.

11. The process of claim 1 wherein said melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether has a melt viscosity in the range of about 5×10 2 Pa·S to about 5×10 4 Pa·S.

12. The process of claim 1 wherein said melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether has a melt viscosity in the range of about 1×10 2 Pa·S to about 3.5×10 4 Pa·S.

13. The process of claim 1 wherein said agitation of said contents of said reaction vessel is sufficient to coagulate greater than about 90% by weight of said melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether.

14. The process of claim 1 wherein said agitation of said contents of said reaction vessel is sufficient to coagulate greater than about 95% by weight of said melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether.

15. The process of claim 1 wherein said agitation of said contents of said reaction vessel is sufficient to coagulate greater than about 98% by weight of said melt-fabricable tough copolymer of tetrafluoroethylene and fluorinated vinyl ether.

16. The process of claim 1 wherein said copolymerizing is carried out by providing a precharge comprising tetrafluoroethylene, fluorinated vinyl ether and telogen in said reaction vessel and introducing additional tetrafluoroethylene to said reaction vessel as said polymerizing proceeds, said telogen being present in a concentration of about 0.1 mole % to about 20 mole % based upon total tetrafluoroethylene and telogen present in said precharge.

17. The process of claim 16 wherein additional fluorinated vinyl ether is added to the reaction vessel as said copolymerizing proceeds.

18. The process of claim 1 wherein said fluorinated vinyl ether is perfluoro(alkyl vinyl ether) and the alkyl group contains 1 to 6 carbon atoms.

19. The process of claim 18 wherein said perfluoro(alkyl vinyl ether) is perfluoro(propyl vinyl ether).

20. The process of claim 18 wherein said perfluoro(alkyl vinyl ether) is perfluoro(ethyl vinyl ether).

21. The process of claim 18 wherein said perfluoro(alkyl vinyl ether) is perfluoro(methyl vinyl ether).

22. The process of claim 18 wherein said perfluoro (alkyl vinyl ether) is perfluoro(methyl vinyl ether) and perfluoro(propyl vinyl ether).

23. The process of claim 1 wherein at least some of said fluorinated vinyl ether is added to said reaction vessel as said copolymerizing proceeds.

Assignments (4)
RELEASE OF SECURITY INTEREST Recorded Apr 4, 2018
From: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 045845/0913 →
SECURITY AGREEMENT Recorded Jun 10, 2015
From: THE CHEMOURS COMPANY FC LLC; THE CHEMOURS COMPANY TT, LLC
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 035839/0675 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 15, 2015
From: E. I. DU PONT DE NEMOURS AND COMPANY
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 035432/0023 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 29, 2004
From: ATEN, RALPH MUNSON
To: E.I. DU PONT DE NEMOURS AND COMPANY
Reel/Frame 014796/0110 →