Novel high-performance forward-penetration film and preparation method thereof
A forward osmosis membrane, high-performance technology, applied in semi-permeable membrane separation, chemical instruments and methods, osmosis/dialysis water/sewage treatment, etc., can solve internal concentration polarization, do not have high water flux and low Salt backdiffusion flux and other issues
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[0045] In the preparation method of the novel high-performance forward osmosis membrane provided by the embodiment of the present invention, it specifically includes:
[0046] Preparation of casting solution: take a certain amount and a certain molecular weight of phenolphthalein side group polyarylether ketone, anhydrous Na 2 SO 4 and concentrated H 2 SO 4 , Stir the reaction at a certain temperature for 6-12 hours. After the reaction, the reaction solution was cooled to room temperature, the product was precipitated with distilled water, and then the precipitate was washed with a large amount of deionization until the pH value was close to 7, and then placed in an electric constant temperature blast drying oven for drying. After mixing and dissolving a certain amount of sulfonated product, polyvinylpyrrolidone, acetone, N,N-dimethylformamide, dimethyl sulfoxide and N-methylpyrrolidone, a casting solution is obtained.
[0047] Pretreatment of the support layer: use a cert...
Embodiment 1
[0066] Stir 80wt% of N,N-dimethylpyrrolidone, 18wt% of SPEK-C and 2wt% of polyvinylpyrrolidone K-30 until completely dissolved, and let stand until defoaming is complete. Dip-coat the casting solution on nylon cloth soaked with N,N-dimethylpyrrolidone, dry at 50°C for 2 hours, dry and cool, then soak the film in deionized water for 24 hours at a constant temperature, and change the water during the period 2 times to ensure that the porogen is removed and the membrane required for the experiment is obtained.
[0067] Using 2mol / L NaCl solution as the driving solution, deionized water as the raw material solution, and the fluid flow rate on both sides of the membrane at 0.25L / min, the separation performance of the prepared forward osmosis composite membrane was tested, and the water flux was 120.65L. m -2 h -1 ; Salt back diffusion flux is 22.28g m -2 h.
Embodiment 2
[0069] 84wt% of N,N-dimethylformamide, 12wt% of SPEK-C and 4wt% of acetone were stirred until completely dissolved, and allowed to stand until defoaming was complete. Dip-coat the casting solution on nylon cloth soaked with N,N-dimethylformamide, dry at 70°C for 3 hours, dry and cool, then soak the film in deionized water for 36 hours at a constant temperature, and replace it during the period. Water was added 4 times to ensure that the porogen was removed to obtain the membrane required for the experiment.
[0070] Using 2mol / L NaCl solution as the driving solution, deionized water as the raw material solution, and the fluid flow rate on both sides of the membrane at 0.25L / min, the separation performance of the prepared forward osmosis composite membrane was tested, and the water flux was 113.65L. m -2 h -1 ; Salt back diffusion flux is 28.31g m -2 h.
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