Method for preparing composite nanofiltration membrane by interfacial polymerization based on step-by-step spin-coating method
A composite nanofiltration membrane and interfacial polymerization technology, applied in the field of nanofiltration membranes, can solve problems such as shortage, achieve the effects of improving utilization rate, simplifying steps, and reducing reaction time
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Embodiment 1
[0029] The present invention a kind of method based on interfacial polymerization of step-by-step spin coating method to prepare composite nanofiltration membrane, comprises the following steps:
[0030] a. the ratio of preparation m-phenylenediamine, hyperbranched polyethyleneimine and water is 0g: 2g: 98g aqueous phase solution, and the ratio of preparation trimesoyl chloride and n-hexane is 1g: 99g organic phase solution;
[0031] b. Place the commercialized polyvinylidene fluoride (PVDF) microporous filter membrane on the spin-coating apparatus plate support, set the rotation speed of the spin-coating apparatus to run at a constant speed of 2000r / min, and drop 1mL of the aqueous phase solution to the polyvinyl Vinylidene fluoride-based film center, and continue to spin for 40s until the aqueous solution is evenly spin-coated;
[0032] c. Then add 1mL of the organic phase solution dropwise to the center of the polyvinylidene fluoride base film at a constant speed within 10s...
Embodiment 2
[0040] Compared with embodiment 1, this embodiment differs in that:
[0041] The rotational speed of the spin coater in step b of Example 1 was adjusted to 4000r / min, and the rest of the process parameters were the same as in Example 1. The separation performance (methylene blue / ethanol mixed solution) of the prepared composite membrane was evaluated using the same nanofiltration test device, test conditions and methods as in Example 1. The results show that the permeate flux of the membrane is 3.6Lm -2 h -1 bar -1 , The rejection rate of methylene blue is 95.4%.
Embodiment 3
[0043] Compared with embodiment 1, this embodiment differs in that:
[0044] The ratio of m-phenylenediamine, hyperbranched polyethyleneimine and water in step a of Example 1 is adjusted to 1.6g: 0.4g: 98g, and the ratio of trimesoyl chloride to n-hexane is adjusted to 0.5g: 99.5g, All the other processing parameters are with embodiment 1. The separation performance (methylene blue / ethanol mixed solution) of the prepared composite membrane was evaluated using the same nanofiltration test device, test conditions and methods as in Example 1. The results show that the permeate flux of the membrane is 2.7Lm -2 h -1 bar -1 , The rejection rate of methylene blue is 98.8%.
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