Anti-pollution ultrafiltration membrane and preparation method thereof
An ultrafiltration membrane and anti-pollution technology, applied in the field of anti-pollution ultrafiltration membrane and its preparation, can solve the problems of high irreversible pollution index, rapid water flux decay, poor anti-pollution performance, etc. The effect of reducing the decay rate and increasing the pollution resistance
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Embodiment 1
[0031] The specific preparation process of the anti-fouling ultrafiltration membrane is as follows:
[0032] Step 1: Incorporate macrocyclic amphiphilic β-CD molecules into 25kg of membrane material polyvinylidene fluoride (PVDF), mix thoroughly by ultrasonication for 30 minutes, then dry the CD / PVDF mixed material under vacuum for 24 hours, and β-CD The mass percentages added are respectively 0%, 1%, and 5% (wt) of the PVDF membrane raw material, and the specific experimental results are shown in Table 1 below;
[0033] Step 2: After mixing 50kg of solvent DMAC with the PVDF raw material in the above step, react at 60°C for 6-8h, let it stand for defoaming, and use the phase inversion method to obtain an anti-pollution film.
[0034] Table 1 Membrane performance comparison
[0035] Membrane type 0% 5% 1% Water flux (L / m 2 h)
[0036] Through comparative experiments, the anti-fouling performance and separation performance of the membrane were investigated. ...
Embodiment 2
[0038] The specific preparation process of the anti-fouling ultrafiltration membrane is as follows:
[0039] Step 1: Sonicate 15kg of film raw material polyvinylidene fluoride (PVDF) for 30 minutes, and dry it under vacuum for 24 hours;
[0040] Step 2: Mix PR and 70kg of solvent DMAC, and carry out ultrasonic dispersion in a conical flask at room temperature for 1 hour to form a uniform and stable solution. After mixing with the PVDF raw material in the above step, react at 60°C for 6-8 hours. Stand for defoaming, and use the phase inversion method to obtain the anti-fouling film, wherein the mass percentage of PR added is 0%, 1%, 2%, 3% (wt) of the solvent DMAC, and the specific results are shown in Table 2 below.
[0041] Table 2 Membrane performance comparison
[0042] Membrane type 0% 1% 2% 3% Water flux (L / m 2 h)
362.5 467.6 623.7 558.2 Retention rate (%) 51.3 62.4 60 75 Strength (Mpa) 2.75 3.05 2.85 3.35
[0043] From th...
Embodiment 3
[0046] The specific operation steps are the same as in Example 2, except that the ultrasonic time in step 1 is 80 min.
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