Preparation method of high-flux porous membrane
A porous membrane and high-flux technology, applied in the field of membrane separation, can solve the problem of small increase
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Embodiment 1
[0030] Add 9g of polyethersulfone and 1.5g of calcium chloride (as an additive) into 39.5g of N,N-dimethylformamide (DMAC, as a solvent), and wait until completely dissolved to form a uniform and stable membrane solution. The film liquid is salivated onto the non-woven fabric with a scraper, and the thickness of the film before gelation is controlled by a metal wire tied on the scraper, and the diameter of the metal wire is 0.235mm in this example. The non-woven fabric with the film liquid is quickly put into the gel bath, the composition of the gel bath is 20wt.% sodium carbonate aqueous solution, and the temperature of the gel bath is 30°C. , the additive will chemically react with the gel medium to form calcium carbonate precipitates. After the membrane gel is formed, the membrane is washed with water and then post-treated. Soak the membrane in 0.5wt% dilute hydrochloric acid at 40°C and take it out after 5 hours. The cross-section of the obtained porous membrane is shown...
Embodiment 2
[0033] The same film-making process, post-treatment and measurement methods as in Example 1, except that the polymer is polyacrylonitrile. The pure water flux and rejection rate of the membrane are 530l / m 2 .h and 90%. The cross-section of the obtained porous membrane is shown in figure 2 .
Embodiment 3
[0035] The same film-making process, post-treatment and measurement methods as in Example 2, except that the gel bath is a 20wt.% potassium carbonate aqueous solution. The pure water flux and rejection rate of the membrane are 480l / m 2 .h and 90%.
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