A high-throughput positively charged nanofiltration membrane and preparation method thereof
A technology for positively charged and nanofiltration membranes, applied in the field of high-throughput positively charged nanofiltration membranes and their preparation, can solve the problems of the preparation time and low water flux of positively charged nanofiltration membranes, and achieve low production costs , short preparation time and good reproducibility
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[0052] The novel high-flux positively-charged nanofiltration membrane of the present invention is obtained by a novel high-flux positively-charged nanofiltration membrane preparation method, and the preparation method comprises the following steps:
[0053] S1: Prepare aqueous solution: add surfactant and proton acceptor to the aqueous solution containing hydrophilic amine monomers, and mix evenly; the hydrophilic amine monomer is 2,4-diamino-6-benzene yl-1,3,5triazine, 1,3-bis(aminomethyl)cyclohexane, tris(hydroxymethyl)aminomethane, N-aminophthalimide and 2,4-dimethyl At least one of oxybenzylamine; the mass concentration of the hydrophilic amine monomer in the aqueous solution is 0.5%-5%; the mass concentration of the proton acceptor in the aqueous solution is 1%-5% ; The mass concentration of the surfactant in the aqueous solution is 0.1%-5%; preferably 0.1%-3%;
[0054] S2: Immerse the porous support layer in the aqueous phase solution, let stand for 30-90s, and remove t...
Embodiment 1
[0062] A novel preparation method of high-flux positively charged nanofiltration membrane:
[0063] S1: Configure the aqueous phase solution: add trisodium phosphate and sodium dodecyl sulfate to the aqueous solution of N-aminophthalimide, and mix evenly; N-aminophthalimide in the aqueous phase solution The mass concentration of sodium lauryl sulfate is 0.5%, the mass concentration of trisodium phosphate is 3%, and the mass concentration of sodium lauryl sulfate is 3%;
[0064] S2: Immerse the porous support ultrafiltration bottom membrane in the aqueous phase solution of S1 for 60s, and remove the excess water phase solution on the surface of the porous support ultrafiltration bottom membrane with rollers; then immerse the porous support layer in the oil phase solution containing acid chloride monomers for 20s. interface reaction, take out and drain off the excess oil phase solution on the surface of the membrane, continue to heat treatment at 90 ° C for 4 min, and spray extr...
Embodiment 2
[0066] A novel preparation method of high-flux positively charged nanofiltration membrane:
[0067] In step S1, the mass concentration of sodium lauryl sulfate is 0.1%;
[0068] The rest of the steps are the same as in Example 1.
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