초록

Porous hydrophilic membranes comprising a porous inert support on which an ionomer is deposited, said membranes being characterized in that they have an ionic conductivity and a water permeability higher than 1 l/(h.m2.Atm).

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1. Porous hydrophilic membranes comprising a porous inert support on which an ionomer is deposited, said membranes being characterized in that they have an ionic conductivity in electrochemical cells and a water permeability higher than 1 l/(h.m2.Atm); the ionomer being under amorphous form and havi

1. Porous hydrophilic membranes comprising a porous inert support on which an ionomer is deposited, said membranes being characterized in that they have an ionic conductivity in electrochemical cells and a water permeability higher than 1 l/(h.m2.Atm); the ionomer being under amorphous form and having the hydrophilic group in the acid form.2. Membranes according to claim 1, having pores partially or totally occluded to gases.3. Membranes having pores totally occluded to gases according to claim 1, containing an ionomer amount higher than about 30% by weight.4. Membranes having pores partially occluded to gases according to claim 1, containing an ionomer amount lower than about 20% by weight.5. Membranes according to claim 1, wherein the porous support is formed by (per)fluoropolymers, preferably PTFE, still more preferably bistretched PTFE.6. Membranes according to claim 1, wherein the ionomers are (per)fluorinated polymers and they optionally have SO3H and/or ?COOH, and or SO3H, functionality, and an equivalent weight such as to result amorphous.7. Membranes according to claim 6, wherein the ionomers comprise:(A) monomeric units deriving from one or more fluorinated monomers containing at least one ethylene unsaturation; (B) fluorinated monomeric units containing functional groups transformable into hydrophilic groups preferably ?SO2F and/or COOR, COF, wherein R is a C1-C20 alkyl radical or a C6-C20 aryl radical, in such an amount to give the above equivalent weight, the functional groups being converted into hydrophilic groups, or into ?SO3H and/or ?COOH groups in the final membrane if the functional groups were ?SO2F and/or ?COOR, ?COF. 8. Membranes according to claim 7, wherein the fluorinated monomers of type (A) are selected from the following:vinylidene fluoride (VDF); C2-C8 perfluoroolefins, or tetrafluoroethylene (TFE); C2-C8 chloro- and/or bromo- and/or iodo-fluoroolefins, and/or chlorotrifluoroethylene (CTFE) and/or bromotrifluoroethylene; CF2?CFORf (per) fluoroalkylvinylethers (PAVE), wherein Rf is a C1-C6 (per) fluoroalkyl, or trifluoromethyl, bromodifluoromethyl, or pentafluoropropyl; CF2?CFOX perfluoro-oxyalkylvinylethers, wherein X is a C1-C12 perfluoro-oxyalkyl having one or more ether groups, or perfluoro-2-propoxy-propyl. 9. Membranes according to claim 7, wherein the fluorinated monomers of type (B) are selected from the following:F2C?CF?O?CF2?CF2?SO2F; F2C?CF?O?[CF2?CXF?O]n?CF2?CF2?SO2F wherein X=Cl, F or CF3; n=1-10; F2C?CF?O?CF2?CF2?CF2?SO2F F2C?CF?Ar?SO2F wherein Ar is an aryl ring; F2C?CF?O?CF2?CF2?CF2?COF F2C?CF?O?[CF2?CXF?O]n?CF2?CFX?COF wherein X=Cl, F or CF3; n=1-10. 10. Membranes according to claim 1, wherein the ionomers contain from 0.01 to 5% by moles of monomeric units deriving from a bis-olefin of formula:R1R2C?CH?(CF2)m?CH?CR5R6??(I) wherein: m=2-10, preferably 4-8; R1, R2, R5, R6, equal to or different from each other, are H or C1-C5 alkyl groups. 11. Membranes according to claim 1, wherein the ionomers comprise:monomeric units deriving from TFE; monomeric units deriving from CF2?CF?O?CF2CF2SO2F; monomeric units deriving from the bis-olefin of formula (I); iodine atoms in end position. 12. Membranes according to claim 1, wherein the amorphous ionomer shows a substantial absence of crystallinity.13. Membranes according to claim 1, wherein the amorphous ionomer has a residual crystallinity lower than 5%.14. Membranes according to claim 1, wherein the (per)fluorinated ionomers are crosslinked.15. Membranes according to claim 1, containing one or more amorphous or crystalline (per)fluoropolymers, the amorphous ones being different from the ionomer used in the membrane.16. Membranes according to claim 15, wherein the (per) fluoropolymers are of crystalline ionomeric type.17. Electrochemical cells operated by the membranes of claim 1.18. Fuel cells operated by the membranes of claim 1.19. Fuel cells according to claim 18, wherein the membranes have pores partially occluded to gases, and certain ionomer amount lower than about 20% by weight, and wherein the air pressure at the cathode side is higher than that of the hydrogen at the anode side, the fed hydrogen coming from reforming.20. A process for preparing hydrophilic porous membranes according to claim 1, comprising a porous support formed by a (per)fluorinated polymer, and amorphous (per)fluorinated ionomers containing hydrophilic groups, preferably having a ?SO3H or ?COOH functionality, said process comprising the following steps:a) impregnation of the porous support formed by the (per)fluorinated polymer, with a (per)fluorinated ionomer having hydrolyzable functions, preferably ?SO2F, ?COOR, ?COF, wherein R is a C1?C20 alkyl radical or a C6-C20 aryl radical, using a solution of the ionomeric compound in fluorinated organic solvent at a concentration in the range 1-20% by weight until obtaining a membrane having the pores substantially filled by the ionomeric solution, the impregnation is carried out at temperatures between the room temperature and 120° C.; the so impregnated membrane is subjected to thermal treatment at temperatures from 50° to 200° C., until substantial removal of the solvent and obtainment of a substantially transparent membrane, optionally step a) is repeated until the membrane appears substantially transparent; b) treatment of the membrane obtained in a) with inorganic strong, optionally aqueous, alkalis, or bases which are completely dissociated in water, to obtain the conversion of the functional groups into hydrophilic groups, optionally from ?SO2F into ?SO3?, and of the ?COOR, ?COF groups into ?COO? groups; c) treatment of the membrane obtained in b) with inorganic strong acids, or acids which are completely dissociated in aqueous solution, obtaining the (per)fluorinated ionomer in acid hydrophilic form; d) optionally treatment with water at temperatures in the range 50° C.-100° C., in case repeated, until removal of the ionomer in excess and neutral pH of the washing waters. 21. A process according to claim 20, wherein in step a) the solvent has a boiling point at room pressure lower than 180° C.22. A process according to claim 20, wherein in step b) the used strong alkales are the hydroxides of the Group Ia metals.23. A process according to claim 20, wherein at the end of step b) washings with water are carried out until a neutral pH of the washing waters is obtained.24. A process according to claim 20, wherein the ionomer is crosslinked by adding to the impregnation solution a) crosslinking agents.25. A process according to claim 24, wherein crosslinking takes place by adding peroxides to the impregnation solution and operating at temperatures from 100 to 300° C.