A kind of preparation method of stable high flux ultrafiltration membrane
An ultrafiltration membrane with high stability technology, applied in the field of stable high-flux ultrafiltration membrane preparation, can solve the problems of enrichment of hydrophobic segments, adverse effects of modification effect, etc., and achieve stable high flux and good separation performance Effect
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Embodiment 1
[0017] Embodiment 1, prepare stable high flux ultrafiltration membrane, the steps are as follows:
[0018] Step 1, preparation of modifier precursor: dissolve maleic anhydride and N-vinylpyrrolidone in a certain amount of N,N-dimethylformamide, use azobisisobutyronitrile as the initiator, at 70 Under ℃, carry out free radical alternating copolymerization for 3 hours, then add styrene to continue polymerization for 3 hours, and finally obtain the structure of poly(N-vinylpyrrolidone-alt-maleic anhydride)-b-polystyrene-like block copolymer (maleic anhydride) The feeding ratio of acid anhydride, N-vinylpyrrolidone and styrene is 1:1:4);
[0019] Step 2. In-situ synthesis of modifier and preparation of stable high-flux ultrafiltration membrane: 100 mg of modifier precursor prepared in step 1, 600 mg of polyethylene glycol 2000, 1600 mg of polyethersulfone and N,N- 7700 mg of dimethylformamide (mass ratio 1:6:16:77) was mixed into a homogeneous solution, stirred at 60°C for 12 hou...
Embodiment 2
[0021] Example 2, the preparation of a stable high-flux ultrafiltration membrane, the preparation process is basically the same as in Example 1, the only difference is that in step 2, the modifier precursor, polyethylene glycol 2000, polyethersulfone and N,N -The mass ratio of dimethylformamide was changed to 1.5:6:16:76.5 to finally obtain a stable high-flux ultrafiltration membrane 2.
[0022] The stable high flux ultrafiltration membrane 2 that embodiment 2 makes is 289Lm in pure water specific flux -2 h -1 bar -1 , the rejection rate of 1g / L bovine serum albumin aqueous solution is 97%, and the flux recovery rates of three cycles are 79.1%, 93.0% and 96.7% respectively.
Embodiment 3
[0023] Example 3, the preparation of a stable high-flux ultrafiltration membrane, the preparation process is basically the same as in Example 1, the only difference is that in step 2, the modifier precursor, polyethylene glycol 2000, polyethersulfone and N,N -The mass ratio of dimethylformamide was changed to 2:6:16:76 to finally obtain a stable high-flux ultrafiltration membrane 3.
[0024] The stable high flux ultrafiltration membrane 3 that embodiment 3 makes is 316Lm in pure water specific flux -2 h -1 bar -1 , the rejection rate of 1g / L bovine serum albumin aqueous solution is 97%, and the flux recovery rates of three cycles are 75.0%, 98.2% and 100.0% respectively. figure 2 The three-cycle flux change diagram for the stable high-flux ultrafiltration membrane 3 filtering 1g / L bovine serum protein solution.
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