Anion exchange membrane and preparation method thereof
An anion exchange membrane and film coating technology, applied in the field of anion exchange membrane and its preparation, can solve the problems of economic consumption, environmental pollution, high production cost, cost increase, etc., achieve outstanding economic and environmental benefits, and simple membrane production process. Effect
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Embodiment 1
[0024] Dissolve 1g of chloromethylated polyethersulfone in a mixed solution of 3g of chloromethylstyrene and 0.3g of divinylbenzene, then add 0.3g of azobisethylbutyronitrile and 1.2g of imidazole and stir evenly, and cast the obtained The membrane solution was scraped on the glass fiber cloth, and then heated and polymerized at 60° C. for 48 hours to obtain an anion exchange membrane. The anion exchange capacity of the membrane was measured to be 2.05 mmol / g.
[0025] The diffusion dialysis performance of the membrane was tested by the method of Comparative Example 1. The results showed that at 25° C., the acid dialysis coefficient of the anion exchange membrane prepared in this example was 0.035 m / h, and the acid / salt separation factor was 60.9. Compared with the anion exchange membrane prepared in Comparative Example 1, the anion exchange membrane prepared in this example has a similar ion exchange capacity, that is, the number of ion exchange sites of the two is similar, bu...
Embodiment 2
[0028] Dissolve 1g of chloromethylated polyethersulfone in a mixed solution of 1g of chloromethylstyrene and 0.02g of divinylbenzene, then add 0.02g of azobisethylbutyronitrile and 0.4g of imidazole and stir evenly, and cast the obtained The membrane solution was sprayed on the nylon cloth, and then heated and polymerized at 90° C. for 6 hours to obtain an anion exchange membrane. The anion exchange capacity of the membrane was measured to be 1.84 mmol / g.
[0029] The diffusion dialysis performance of the membrane was tested by the method of Example 1. The results showed that at 25° C., the acid dialysis coefficient of the membrane prepared in this example was 0.014 m / h, and the acid / salt separation factor was 82.5. It can be seen that the anion exchange membrane prepared by the present invention has excellent diffusion dialysis performance and can be used in the field of waste acid recovery.
Embodiment 3
[0031] This example adopts the same operation process as Example 1, the only difference is that the casting liquid is dipped into the coating film on the polyester cloth to obtain an anion exchange membrane with similar structure and performance, which can be used in the field of waste acid recovery.
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