MOF-199@PVDF matrix blend membrane having high pollution resistance, and production method thereof
A technology of MOF-199 and blended membranes, applied in chemical instruments and methods, membranes, membrane technology, etc., can solve membrane fouling, shorten service life, affect membrane separation performance and other problems, achieve high rejection rate, small adsorption, Good anti-pollution effect
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specific Embodiment approach 1
[0018] Specific embodiment 1: Add 5wt% (mass percentage relative to PVDF) MOF-199 additive into 74wt% dimethylformamide solvent, then ultrasonically disperse for 0.5 hours, and then add it in a vacuum drying oven under the condition of 85°C The 16wt% polyvinylidene fluoride dried for 10 hours was continuously stirred in a constant temperature water bath at 70°C, and the porogen was added after 1 hour to continue stirring for a total of 6 hours, and then left to stand for defoaming for 12 hours. Apply the casting solution evenly on a clean glass plate at room temperature, the thickness of the thread of the scraping rod is 200 μm, then immerse the glass plate in a 25°C water bath, peel the resulting film from the glass plate and immerse it in deionized water for 3 days To remove residual solvent and non-solvent additives. Its pure water flux reaches 84.73L / m 2 h, the bovine serum albumin retention rate reaches 95%. Backwashing the matrix blend membrane contaminated by bovine s...
specific Embodiment approach 2
[0019] Embodiment 2: This embodiment is different from Embodiment 1 in that: N-methyl-2-pyrrolidone is used as the solvent. Other steps and parameters are the same as in the first embodiment. The pure water flux of the prepared flat membrane reaches 78.33L / m 2 h, the bovine serum albumin retention rate reaches 97%. Backwashing the matrix blend membrane contaminated by bovine serum albumin, the recovery water flux reaches 48.63L / m -2 h.
specific Embodiment approach 3
[0020] Embodiment 3: This embodiment differs from Embodiment 1 in that the content of the additive MOF-199 is 3 wt%, and other steps and parameters are the same as Embodiment 1. The pure water flux of the prepared flat membrane reaches 82.42L / m 2 h, bovine serum albumin rejection rate reached 96%, backwashed the matrix blended membrane after bovine serum albumin contamination, and the recovery water flux reached 53.21L / m 2 h.
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