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A continuous process for applying subgaskets to surfaces of CCM subassemblies, comprising: a) preparation of a roll (A), wherein on each of two surfaces, electrocatalytic layers longitudinally distributed at regular intervals are applied;b) preparation of two subgasket rolls (B) wherein, on a subgas

A continuous process for applying subgaskets to surfaces of CCM subassemblies, comprising: a) preparation of a roll (A), wherein on each of two surfaces, electrocatalytic layers longitudinally distributed at regular intervals are applied;b) preparation of two subgasket rolls (B) wherein, on a subgasket sheet, in correspondence to the position of the electrocatalytic layers in the roll (A), openings are made; the percent ratio (subgasket opening area)/(electrocatalytic layer area) being between 90% and 99%;c) hot lamination of two rolls (B) with the roll (A); the step being carried out so that the perimeter of the openings of the two rolls (B) falls inside the area of the electrocatalytic layers, and obtaining a roll (C), wherein on each of the two surfaces of the sheet formed of a CCM sequence (roll (A)) a subgasket sheet (roll (B)) is applied.

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1. A continuous process for preparing catalyst coated membrane (CCM) assemblies with subgaskets on both CCM sides, comprising the following steps: a) providing an ionomeric membrane sheet that is free of electrocatalytic layers;b) preparing an internal layer comprising a composite comprising a centr

1. A continuous process for preparing catalyst coated membrane (CCM) assemblies with subgaskets on both CCM sides, comprising the following steps: a) providing an ionomeric membrane sheet that is free of electrocatalytic layers;b) preparing an internal layer comprising a composite comprising a central layer formed of the ionomeric membrane sheet having an electrocatalytic layer positioned on each side only at longitudinally symmetrical regular intervals;c) preparing two surface layers comprising a subgasket sheet, wherein the subgasket sheet has openings corresponding to the position of the electrocatalytic layers of the internal layer; wherein the ratio of the subgasket sheet opening area to the electrocatalytic layer area is between 90% and 99%; andd) hot laminating the two surface layers onto the internal layer by simultaneously feeding the internal layer between the two surface layers between two drums so that the perimeter ofthe subgasket sheet openings of the two surface layers falls inside the area of the electrocatalytic layers,wherein the two surface layers are applied to the internal layer using one of the following processes:i. adhesivizing the two surface layers on the side to be in contact with the internal layer with a hot melt adhesive prior to hot laminating, andii. adhesivizing the two surface layers on the side to be in contact with the internal layer with a pressure-sensitive adhesive prior to hot laminating. 2. A process according to claim 1, wherein the two surface layers have the same width as the internal layer. 3. A process according to claim 1, wherein the two surface layers comprise hydrogenated and/or fluorinated thermoplastic polymer sheets. 4. A process according to claim 1, wherein process i is used. 5. A process according to claim 4, wherein the hot melt adhesive is ethylene vinyl acetate (EVA). 6. A process according to claim 1, wherein in step d) the hot lamination is carried out under the following conditions: a roll progress rate of 0.1-5 m/min;pressure on the sheets to be laminated of 5-40 kg/cm2; anda temperature higher than 100° C. and not higher than 150° C. 7. A process according to claim 1, wherein a lamination temperature between 100° C. and 130° C. is used when the two surface layers are formed of polyethyleneterephthalate (PET) adhesivized with ethylene vinyl acetate (EVA). 8. A process according to claim 1, wherein the ionomeric membrane sheet and the electrocatalytic layers of the internal layer are obtained using (per) fluorinated ionomers with —SO3H groups and/or —COOH groups in acid or neutralized form, having an equivalent weight from 380 to 1,600 g/eq. 9. A process according to claim 8, wherein the ionomers comprise the following units: (A) monomeric units derived from one or more fluorinated monomers containing at least one ethylenic unsaturation; and at least one of:(B) fluorinated monomeric units containing sulphonyl groups —SO2F in amounts such that the ionomer has the equivalent weight in the above range and(B′) monomeric units containing precursor groups which are transformed by hydrolysis into acid groups —COOH, optionally their subsequent salification, in amounts such that the ionomer has the equivalent weight in the above range. 10. A process according to claim 8, wherein the ionomers are homopolymers formed of fluorinated monomeric units (B) containing sulphonyl groups —SO2F, the ionomers containing the sulphonic groups in acid form —SO3H or salified form being obtained by hydrolysis of the —SO2F groups. 11. A process according to claim 9, wherein the fluorinated monomeric units (A) are selected from the group consisting of: vinylidene fluoride (VDF);C2-C8 perfluoroolefins;C2-C8 chloro- and/or bromo- and/or iodo-fluoroolefins;CF2═CFORf1 (per)fluoroalkylvinylether (PAVE), wherein Rf1 is a C1-C6 (per) fluoroalkyl;CF2═CFOX perfluoro-oxyalkylvinylethers, wherein X is a C1-C12 perfluoro-oxyalkyl having one or more ether groups; andfluorovinylethers (MOVE) of general formula CFXAl═CXAlOCF2ORAl (A-I), wherein RAl is a linear or branched C1-C6 (per) fluoroalkyl group or C5-C6 cyclic, or a linear or branched C1-C6 (per) fluoro-oxyalkyl group containing from one to three oxygen atoms;when RAl is fluoralkyl or fluoro-oxyalkyl as above it can contain from 1 to 2 atoms, equal or different, selected from: H, Cl, Br, and I; and wherein) XAI═F or H. 12. A process according to claim 9, wherein the ionomers comprise monomers (B′) in admixture with monomers (B). 13. A process according to claim 1 wherein the ionomeric membrane comprises ionomers comprising from 0.01% to 2% by moles of monomeric units derived from a bis-olefin of formula: R1R2C═CH— (CF2)m—CH—CR5R6 wherein:m =2−10;R1, R2, R5, R6, are equal to or different from each other, and are H or C1-C5 alkyl groups. 14. A process according to claim 8, wherein the ionomeric membranes and the electrocatalytic layers contain perfluorinated ionomers obtained from ionomers comprising: monomeric units derived from tetrafluoroethylene (TFE);monomeric units derived from CF2═CF—O—CF2CF2SO2F. 15. A process according to claim 8, wherein the ionomers are crosslinked or crosslinkable. 16. A process according to claim 1, wherein the electrocatalytic layers comprise an ionomer and a catalyst. 17. A process according to claim 16, wherein the ratio by weight between catalyst and ionomer in each of the two electrocatalytic layers ranges from 0.5 to 4. 18. A process according to claim 16, wherein the ratio of weight of the catalyst to area of the electrocatalytic layer ranges from 0.01 to 2 mg/cm2.