Oxidation resistant compound reverse osmosis membrane
A reverse osmosis membrane and oxidation-resistant technology, which is applied in the field of water treatment, can solve the problems of reducing membrane operating efficiency, increasing operating costs, and short service life of reverse osmosis membranes, so as to improve oxidation resistance and organic pollution resistance. Chlorine performance and anti-pollution performance are strong and the cleaning interval is long
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Embodiment 1-6
[0018] A porous polysulfone support membrane composed of a DMF solution containing 16% polysulfone was used and placed in a 2.5% m-phenylenediamine (MPDA) solution for about 1 minute. The amine solutions each contained 0.1 wt% sodium dodecylsulfonate (SDBS) surfactant. The support film soaked in MIPA was placed on a paper towel and rolled with a rubber roller to remove excess solution on the front and back. The above steps and the amount of polyamine used are the same as those in the prior art for preparing the polyamide layer. This support layer was then contacted with an organic solution of acid chloride (-COCl) listed in Table 1 containing 0.1% (wt / v%) for 50 seconds, and then placed in a 40°C oven for 10 minutes to form a polyamide layer. After taking it out, use a potassium persulfate solution with a concentration of 1%, and treat it for 30 minutes when the pH of the potassium phosphate buffer solution is 8. Then keep it in an oven at 140° C. for 5 minutes to obtain the...
Embodiment 7
[0024] Except that 2-iodo-terephthaloyl chloride was used instead of 5-iodo-isophthaloyl chloride, a composite reverse osmosis membrane was prepared by the same operation as in Example 4. Then using the same test method as in Example 4, the initial desalination rate of the membrane was 99.1%, and the water flux was 25.3GFD. After NaClO oxidation treatment, the desalination rate was 98.5%, and the water flux was 33.4GFD.
Embodiment 8
[0026] Except that 5-bromo-isophthaloyl chloride was used instead of 5-iodo-isophthaloyl chloride, the same operation as in Example 4 was used to prepare a composite reverse osmosis membrane. Then using the same test method as in Example 4, the initial desalination rate of the membrane was 98.7%, and the water flux was 22.8GFD. After NaClO oxidation treatment, the desalination rate was 97.0%, and the water flux was 34.4GFD.
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