Flow battery diaphragm and its preparation method
A liquid flow battery and diaphragm technology, which is applied in the direction of fuel cells, battery pack components, fuel cell components, etc., can solve the problems of attenuation of vanadium resistance and increase of internal resistance of batteries, etc., and achieve reduced membrane resistance and long working life , Reduce the permeability and the effect of water molecule migration number
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Embodiment 1
[0049] The tetrafluoroethylene with the exchange capacity of 1.35mmol / g and the monomer of formula (V) are copolymerized into perfluorosulfonic acid resin, and its molecular repeating structure is as follows:
[0050]
[0051] The above-mentioned perfluorosulfonic acid resin was extruded through an extruder at 210° C. to extrude a film with a thickness of 50 μm. The above-mentioned extruded film was soaked in 20 wt% ammonia water for 1 min. After taking it out, place it at 250°C for heat treatment to generate cross-linked structures (II) on both sides of the film. Put the crosslinked membrane in 10wt% sodium hydroxide for 80°C hydrolysis for 8 hours, then place it in 5wt% sulfuric acid, keep the temperature at 80°C for 3 hours, wash until neutral, and obtain a crosslinked flow battery diaphragm.
Embodiment 2
[0053] The tetrafluoroethylene with the exchange capacity of 1.00mmol / g and the monomer of formula (III) are copolymerized into perfluorosulfonic acid resin, and its molecular repeating structure is as follows:
[0054]
[0055] Through an extruder, extrude at 250° C., and the extruded thickness is 100 μm. One side of the extruded film was placed in 10 wt% hydrazine solution for 10 min. After taking it out, place the film at 230° C. for 3 hours for heat crosslinking to form a film with a crosslinked structure of n=0 in formula (I). The cross-linked membrane was hydrolyzed in 10% sodium hydroxide at 80° C. for 8 hours to obtain a cross-linked flow battery separator.
Embodiment 3
[0057] The exchange capacity is 1.20mmol / g tetrafluoroethylene and the monomer of formula (III) and the monomer of formula (VI) terpolymerized into perfluorosulfonic acid resin
[0058] Through an extruder, extrude at 190° C., and the extruded thickness is 150 μm. The above extruded film was immersed in 10wt% perfluoromethylenediamine of formula (VII)x=2 for 20min. After taking it out, place the film at 200° C. for thermal crosslinking for 3 hours to form a crosslinked structure with n=2 in formula (I) on both sides of the film. The cross-linked membrane was hydrolyzed in 10% sodium hydroxide at 80° C. for 8 hours to obtain a cross-linked flow battery separator.
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