Method for producing aqueous perfluoroelastomer dispersion, and method for producing perfluoroelastomer
US-2016347895-A1 · Dec 1, 2016 · US
US12018105B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12018105-B2 |
| Application number | US-201917053985-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 8, 2019 |
| Priority date | May 9, 2018 |
| Publication date | Jun 25, 2024 |
| Grant date | Jun 25, 2024 |
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Method of reducing the amount of a fluorinated acid or its salts from a fluoropolymer, the method comprises: (i) providing a composition containing particles of the fluoropolymer, (ii) contacting the fluoropolymer particles with a treatment composition comprising at least one organic liquid; and, optionally, further comprising (iii) isolating, washing and subjecting the fluoropolymer to drying treatment, and wherein the fluoropolymer contains units derived from tetrafluoroethene (TFE) and is selected from the group of fluoroelastomers and the group of fluoropolymers having a melting point of less than 150° C. Also provided are fluoropolymer and compositions containing such polymers that are essentially free of fluorinated acids and their salts.
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The invention claimed is: 1. A method for reducing the amount of a fluorinated acid or its salts from a fluoropolymer, the method comprises (i) providing a composition containing particles of the fluoropolymer, and (ii) contacting the fluoropolymer particles with a treatment composition comprising at least one organic liquid, wherein the organic liquid is immiscible with water at ambient conditions and the composition containing the fluoropolymer comprises a coagulated fluoropolymer; and wherein the fluoropolymer contains units derived from tetrafluoroethene (TFE) and is fluoroelastomer or has a melting point of less than 150° C. 2. The method of claim 1 wherein the composition containing the fluoropolymer is the reaction product of a polymerization reaction to produce the fluoropolymer. 3. The method of claim 1 further comprising (iii) isolating, washing and subjecting the fluoropolymer to drying treatment. 4. The method of claim 1 wherein the fluorinated acid and its salts corresponds to the general formula: Y—R f —Z-M wherein Y represents hydrogen, Cl or F; R f represents a divalent linear or branched or cyclic perfluorinated or partially fluorinated saturated carbon chain having 4 to 18 carbon atoms; Z represents an acid group, for example a —COO − or a —SO 3 − acid group, and M represents a cation. 5. The method of claim 1 wherein the fluorinated acid is a perfluorooctanoic acid or its salt and wherein its amount is reduced to, less than 25 ppb, based on the weight of the fluoropolymer. 6. The method of claim 1 wherein the composition is an aqueous dispersion and the process comprises (iv) reducing the pH of the aqueous composition by adding one or more mineral acids and wherein (iv) is carried out prior to and/or simultaneous with (ii). 7. The method of claim 1 wherein the composition is an aqueous dispersion and the process further comprises (v) coagulating the fluoropolymer and wherein (v) is carried out prior to (ii) or simultaneously with (ii). 8. The method of claim 1 wherein the extractable fluorinated acid is a perfluorinated acid selected from C 9 -C 14 alkanoic carboxylic acids and wherein the total amount of these acids is reduced to less than 100 ppb, based on the weight of the fluoropolymer. 9. The method of claim 1 wherein the fluoropolymer contains units derived from one or more comonomers selected from unsaturated perfluorinated ethers according to the general formula: R f —O—(CF 2 ) n —CF═CF 2 wherein n is 1 (allyl ether) or 0 (vinyl ether), and Rf represents a linear or branched perfluoroalkyl residue containing from 1 to 10 carbon atoms which may be interrupted once or more than once by an oxygen atom. 10. The method of claim 1 wherein the fluoropolymer is a curable fluoroelastomer and is essentially free of ionic end groups and contains ionic end groups in such an amount that the absorbance ratio determined by calculating the integrated peak intensity within the range of 1840 cm −1 -1620 cm −1 to the integrated peak intensity in the range 2740 cm −1 -2220 cm −1 in a Fourier-transform infrared spectrum of the polymer, is less than 0.1. 11. The method of claim 1 wherein the fluoropolymer is a fluoroelastomer and the organic liquid has a boiling point of from 30 to 200° C. 12. The method of claim 1 wherein the organic liquid is a hydrocarbon that may, optionally, contain one or more functional groups selected from halogen atoms, ether groups, carboxylate ester groups, phosphoric acid ester groups, phosphonic acid ester groups, sulfonic acid ester groups, sulfuric acid ester groups, nitrile groups, ketone groups, carbon-carbon double bonds, carbon-carbon triple bonds, hydroxy groups, nitrogen-containing functional groups other than nitrile groups, sulfoxide groups, anhydride groups and combinations thereof. 13. The method of claim 1 wherein the composition containing particles of the fluoropolymer has been obtained by subjecting an aqueous dispersion of the fluoropolymer to anion exchange with an anion exchange resin to remove fluorinated sulfonic acids and wherein the anion exchange resin has been loaded with one or more fluorinated acid corresponding to the general formula: [R f —O-L-COO—] i X i+ wherein L represents a linear or branched or cyclic partially fluorinated alkylene (alkanediyl) group or an aliphatic hydrocarbon group, R f represents a linear or branched, partially or fully fluorinated aliphatic group or a linear or branched partially or fully fluorinated group interrupted once or more than once by an ether oxygen atom, X i+ represents a cation having the valence i and i is 1, 2 and 3. 14. A fluoropolymer made by the method of claim 1 , the fluoropolymer having an amount of an extractable fluorinated acid and its salt of less than 100 ppb, based on the weight of the fluoropolymer, wherein the fluorinated acid corresponds to the general formula: Y—R f —Z-M wherein Y represents hydrogen, Cl or F; R f represents a divalent linear or branched or cyclic perfluorinated or partially fluorinated saturated carbon chain having 4 to 18 carbon atoms; Z represents an acid group, for example a —COO − or a —SO 3 − acid group, and M represents a cation. 15. The fluoropolymer of claim 14 having a total amount of perfluorinated alkanoic sulfonic acids having 4 to 8 carbon atoms or its salts of less than 5 ppb, based on the weight of the fluoropolymer. 16. The method of claim 1 wherein the fluoropolymer has a melting point of less 150° C. and the organic liquid has a boiling point of from 30 to below the melting point of the fluoropolymer. 17. The method of claim 4 , wherein the cation is H + . 18. The fluoropolymer of claim 15 , wherein the cation is H + .
Homopolymers or copolymers or tetrafluoroethene · CPC title
with fluorinated vinyl ethers · CPC title
Tetrafluoroethene · CPC title
Purification · CPC title
Coagulation · CPC title
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