Fluoropolymer Produced by Aqueous Polymerization Using Dispersed Particulate of Fluorinated Ionomer Produced In Situ

• US 20100160510A1
• Filed: 12/18/2009
• Published: 06/24/2010
• Est. Priority Date: 12/23/2008
• Status: Active Grant

• Current Assignee: The Chemours Company FC, LLC (The Chemours Company)
• Original Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Inventors: Aten, Ralph Munson, Leffew, Kenneth Wayne, Noelke, Charles Joseph, Lloyd, Ralph Birchard
• Granted Patent: US 8,058,376 B2
• Time in Patent Office: Days
• US Class Current: 524/131
• CPC Class Codes: C08F 14/18 Monomers containing fluorine
• CPC Class Codes: C08F 2/16 Aqueous medium
• CPC Class Codes: C08F 214/18 Monomers containing fluorine
• CPC Class Codes: C08F 259/08 on to polymers containing fluorine

Abstract

A process for making an aqueous dispersion of fluoropolymer particles by polymerizing in a first polymerization step at least one fluorinated monomer having an ionic group in an aqueous polymerization medium in the presence of initiator, the polymerizing providing dispersed particulate of fluorinated ionomer, and polymerizing in a second polymerization step at least one fluorinated monomer in the aqueous polymerization medium in the presence of the dispersed particulate of fluorinated ionomer and initiator to form the aqueous dispersion of particles of fluoropolymer.

Claims

1. A process for making an aqueous dispersion of fluoropolymer particles comprising:

polymerizing in a first polymerization step at least one fluorinated monomer having an ionic group in an aqueous polymerization medium in the presence of initiator, said polymerizing providing dispersed particulate of fluorinated ionomer;

polymerizing in a second polymerization step at least one fluorinated monomer in said aqueous polymerization medium in the presence of said dispersed particulate of fluorinated ionomer and initiator to form the aqueous dispersion of particles of fluoropolymer.

2. The process of claim 1 further comprising suspending said first polymerization step prior to beginning said second polymerization step.

3. The process of claim 1 wherein during said suspending said dispersed particulate of fluorinated ionomer is stored in a separate vessel.

4. The process of claim 1 wherein said first polymerization step produces sufficient dispersed fluorinated ionomer particulate for carrying out said second polymerization step multiple times.

5. The process of claim 1 wherein the amount of said dispersed particulate of fluorinated ionomer present in said aqueous polymerization medium in said second polymerization step comprises less than about 15 wt % of said fluoropolymer solids produced in said aqueous dispersion.

6. The process of claim 1 wherein said particulate of fluorinated ionomer have a weight average particle size of about 2 nm to about 100 nm. The process of claim 1 wherein said fluorinated ionomer has an ion exchange ratio of about 3 to about 53.

7. The process of claim 1 wherein said fluorinated ionomer is highly fluorinated.

8. The process of claim 1 wherein said fluorinated ionomer is perfluorinated.

9. The process of claim 1 wherein said fluorinated ionomer comprises a polymer backbone with recurring side chains attached to the polymer backbone with the side chains carrying ionic groups.

10. The process of claim 1 wherein said fluorinated ionomer comprises ionic groups having a pKa less than about 10.

11. The process of claim 1 wherein said fluorinated ionomer comprises ionic groups selected from the group consisting of sulfonate, carboxylate, phosphonate, phosphate, and mixtures thereof.

12. The process of claim 1 wherein said fluorinated ionomer comprises sulfonate groups.

13. The process of claim 12 wherein said recurring side chains are represented by the formula —

(O—

CF₂CFR_f)_a—

(O—

CF₂)_b—

(CFR′

_f)_cSO₃X, wherein R_f and R′

_f are independently selected from F, Cl or a perfluorinated alkyl group having 1 to 10 carbon atoms, a=0 to 2, b=0 to 1, c=0 to 6, and X is H, Li, Na, K or NH₄.

14. The process of claim 13 wherein said fluorinated ionomer is a copolymer prepared from tetrafluoroethylene and CF₂═

CF₂O—

CF₂CF(CF₃)—

O—

CF₂CF₂—

SO₃X wherein X is H, Li, Na, K or NH₄.

15. The process of claim 1 wherein said fluorinated ionomer in thermoplastic form has a melt flow at 270°

C. using a 5 kg weight of about 1 to about 500.

16. The process of claim 1 further comprising providing surfactant in said polymerization medium.

17. The process of claim 1 further comprising providing fluorosurfactant in said polymerization medium.

18. The process of claim 1 further comprising providing fluoroether surfactant in said polymerization medium.

19. The process of claim 17 wherein said fluorosurfactant has the formula:

[R¹—

O_n-L-A⁻

] Y⁺

wherein;

R¹ is a linear or branched partially or fully fluorinated aliphatic group which may contain ether linkages;

n is 0 or 1;

L is a linear or branched alkylene group which may be nonfluorinated, partially fluorinated or fully fluorinated and which may contain ether linkages;

A⁻

is an anionic group selected from the group consisting of carboxylate, sulfonate, sulfonamide anion, and phosphonate; and

Y⁺ is hydrogen, ammonium or alkali metal cation;

with the proviso that the chain length of R¹—

O_n-L- is not greater than 6 atoms.

20. The process of claim 19 wherein n is 1.

21. The process of claim 20 wherein

R¹ is CF₃CF₂CF₂—

;

L is —

CF(CF₃)—

; and

A⁻

i s carboxylate; and

Y⁺ is hydrogen or ammonium.

22. The process of claim 1 wherein said aqueous medium contains less than about 300 ppm of perfluoroalkane carboxylic acid or salt fluorosurfactant having 8 or more carbon atoms based on the weight of water in said aqueous polymerization medium.

23. The process of claim 1 wherein said polymerizing produces less than about 13 wt % undispersed fluoropolymer based on the total weight of fluoropolymer produced.

24. The process of claim 1 wherein said at least one fluorinated monomer is selected from the group consisting of tetrafluoroethylene (TFE), hexafluoropropylene (HFP), chlorotrifluoroethylene (CTFE), trifluoroethylene, hexafluoroisobutylene, perfluoroalkyl ethylenes, fluorovinyl ethers, vinyl fluoride (VF), vinylidene fluoride (VF2), perfluoro-2,2-dimethyl-1,3-dioxole (PDD), perfluoro-2-methylene-4-methyl-1,3-dioxolane (PMD), perfluoro(allyl vinyl ether) and perfluoro(butenyl vinyl ether).

25. The process of claim 1 wherein said polymerizing of said at least one fluorinated monomer produces polytetrafluoroethylene or modified polytetrafluoroethylene having a comonomer content of no greater than about 1 wt %.

26. The process of claim 1 wherein said polymerizing of said at least one fluorinated monomer produces a melt-processible copolymer comprising at least about 60-98 wt % tetrafluoroethylene units and about 2-40 wt % of at least one other monomer.

27. The process of claim 1 wherein said polymerizing of said at least one fluorinated monomer produces a melt-processible copolymer containing functional groups which are precursors for ionic groups.

28. The process of claim 1 wherein said polymerizing of said at least one fluorinated monomer produces a fluorocarbon elastomer.

29. The process of claim 28 wherein said fluorocarbon elastomer copolymers comprise 25 to 70 wt %, based on total weight of the fluorocarbon elastomer, of copolymerized units of a first fluorinated monomer selected from the group consisting of vinylidene fluoride (VF2), tetrafluoroethylene (TFE), and mixtures thereof.