Fluoroionomers dispersions having a low surface tension, low liquid viscosity and high solid content

1. A process for manufacturing a (per)fluoroionomer liquid composition having a (per)fluoroionomer content of at least 9% wt, with respect to the total weight of the composition, said process comprising:

providing a (per)fluoroionomer (I);

submitting said (per)fluoroionomer (I) to at least one step selected from the group consisting of:

(A) fluorination with elemental fluorine;

(B) treatment with a polar organic solvent (S); and

the combination thereof;

and separating said (per)fluoroionomer (I) to recover a purified (per)fluoroionomer (I);

dispersing said purified (per)fluoroionomer (I) at a temperature of at least 150° C. in an aqueous medium substantially free from organic solvents, to obtain an aqueous composition; and

adding to said aqueous composition at least one polar organic solvent (S′).

2. The process of claim 1 , wherein said fluoroionomer (I) comprises recurring units derived from at least one fluorinated functional monomer selected from the group consisting of:

(M1) sulfonated perfluoroolefin of formula (M1):

wherein n is an integer between 0 and 6 and X′ is selected from the group consisting of halogen, —O − M + , wherein M + is a cation selected from the group consisting of H + , NH 4 + , K + , Li + , Na + , and-mixtures thereof; wherein said halogen is selected from the group consisting of Cl, F, Br, I, and mixtures thereof;

(M2) sulfonated perfluorovinylethers of formula (M2):

wherein m is an integer between 1 and 10 and X′ is selected from the group consisting of halogen, —O − M + , wherein M + is a cation selected from the group consisting of H + , NH 4 + , K + , Li + , Na + , and-mixtures thereof; wherein said halogen is selected from the group consisting of Cl, F, Br, I, and mixtures thereof;

(M3) sulfonated perfluoroalkoxyvinylethers of formula (M3):

wherein w is an integer between 0 and 2,

wherein RF 1 and RF 2 , equal or different from each other and at each occurrence, are independently —F, —Cl or a C 1-10 perfluoroalkyl group, optionally substituted with one or more ether oxygens,

wherein y is an integer between 0 and 6, and

wherein X′ is selected from the group consisting of halogen, —O − M + , wherein M + is a cation selected from the group consisting of H + , NH 4 + , K + , Li + , Na + , and-mixtures thereof; wherein said halogen is selected from the group consisting of Cl, F, Br, I, and mixtures thereof;

(M4) perfluoroalkoxyvinylether carboxylates of formula (M4):

wherein w is an integer between 0 and 2,

wherein y is an integer between 0 and 6,

wherein RF 1 and RF 2 , equal or different from each other and at each occurrence, are independently —F, —Cl or a C 1-10 perfluoroalkyl group, optionally substituted with one or more ether oxygens,

and R H§ is a C 1-10 alkyl or fluoroalkyl group;

(M5) sulfonated aromatic (per)fluoroolefins of formula (M5):

wherein Ar is a C 3-15 aromatic or heteroaromatic moiety and X′ is selected from the group consisting of halogen, —O − M + , wherein M + is a cation selected from the group consisting of H + , NH 4 + , K + , Li + , Na + , and-mixtures thereof; wherein said halogen is selected from the group consisting of Cl, F, Br, I, and mixtures thereof; and

(M6) mixtures thereof.

3. The process of claim 2 , wherein said (per)fluoroionomer (I) is a tetrafluoroethylene copolymer comprising:

from 5 to 30% by moles of recurring units derived from the group consisting of perfluoro-2-(2-fluorosulfonylethoxy)propylvinyl ether (PSEPVE) of formula (M3-A):

perfuoro-5-sulphonylfluoride-3-oxa-1-pentene (SFVE) of formula (M2-D):

in their —SO 2 F form, and their —SO 2 X″ form,

wherein X″ is selected from the group consisting of halogen, —O − M + , wherein M + is a cation selected from the group consisting of H + , NH 4 + , K + , Li + , Na + , and-mixtures thereof;

wherein said halogen is selected from the group consisting of Cl, F, Br, I, and mixtures thereof; and

from 95 to 70% by moles of recurring units derived from tetrafluoroethylene (TFE).

4. The process of claim 1 comprising said fluorination (A) of said (per)fluoroionomer (I), in combination with said solvent (S) treatment (B) and wherein said (per)fluoropolymer (I) is firstly submitted to said solvent (S) treatment (B) and then submitted to said fluorination (A).

5. The process of claim 1 , wherein the (per)fluoroionomer aqueous liquid composition exhibits surface tension of 15 to 30 mN/m, when determined at 25° C., and wherein said (per)fluoroionomer liquid composition possesses a liquid viscosity when determined at 25° C. at a shear rate of 100 sec−1, of:

less than 100 Cpoise, when said (per)fluoroionomer (I) concentration is of at most 15% wt, with respect to the total weight of said liquid composition;

less than 150 Cpoise, when said (per)fluoroionomer (I) concentration is of more than 15% wt and at most 30% wt, with respect to the total weight of said liquid composition; and

less than 200 Cpoise, when said (per)fluoroionomer (I) concentration is of more than 30% wt, with respect to the total weight of said liquid composition.

6. The process of claim 1 , wherein solvent (S′) is selected from the group consisting of methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, isobutanol, ethylene glycol and mixtures thereof.

7. The process of claim 6 , wherein solvent (S′) is selected from the group consisting of 1-propanol, 2-propanol and a mixture thereof.