Preparation method of polyamide composite nanofiltration membrane containing modified carbon nano tube
A composite nanofiltration membrane and carbon nanotube technology, applied in the field of membrane separation, can solve the problems of non-polar organic solvents that are difficult to disperse, limit the application of carbon nanotubes, and be difficult to disperse, so as to achieve easy industrial production and application, improve defects, The effect of enhancing the interaction force
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Embodiment 1
[0040] Take 1g of multi-walled carbon nanotubes (average diameter of 10-30 nanometers, length of 1-2 microns), add 75mL 98% sulfuric acid and 25mL 65% nitric acid (volume ratio 3:1), ultrasonic dispersion at 50 ℃ for 60 minutes, and then 80 The reaction was carried out in a water bath at ℃ for 2 hours, the reaction product was added with 2000 mL of pure water and then filtered with a water membrane with a pore size of 0.22 μm, washed until the filtrate had a pH value of 7, and dried under vacuum at 80 ℃. Scrape the dried carboxylated carbon tube from the wall of the beaker and grind it into powder for later use. The obtained carboxylated carbon tubes are carbon nanotubes treated with mixed acid. See the scanning electron micrograph figure 1 . Dissolve 0.1g of SDS (sodium dodecyl sulfate) in 5mL of water, add 0.1g of carboxylated carbon tube and 1.5g of MMA (methyl methacrylate), sonicate for 30min, and take 0.015g of it and recrystallize it with ethanol. The purified AIBN was ...
Embodiment 2-5
[0042] Example 2-5: The concentration of piperazine in the aqueous medium was adjusted, as shown in Table 1, and the remaining reaction conditions were the same as in Example 1.
[0043] The PMMA-MWNTs aromatic polyamide hybrid nanofiltration membrane prepared in Examples 1-5 was tested for water flux and sodium sulfate rejection. The results are shown in Table 1.
[0044] Examples 1-5 are to investigate the effect of piperazine concentration in the aqueous medium on the water flux and salt rejection rate of the PMMA-modified carbon tube composite nanofiltration membrane.
[0045] Table 1
[0046]
Embodiment 6-9
[0047] Examples 6-9: The concentration of trimesoyl chloride in the organic phase was changed, as shown in Table 2, and the remaining reaction conditions were the same as in Example 1.
[0048] The PMMA-MWNTs aromatic polyamide hybrid nanofiltration membrane prepared in Examples 6-9 was tested for water flux and sodium sulfate rejection. The results are shown in Table 2. Examples 6-9 are to investigate the influence of the concentration of trimesoyl chloride in the oil phase medium on the water flux and salt rejection rate of the PMMA-modified carbon tube composite nanofiltration membrane.
[0049] Table 2
[0050]
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