Preparation method of ultrahigh-flux composite nanofiltration membrane
A technology of composite nanofiltration membrane and ultrafiltration membrane, which is applied in the field of membrane separation, can solve problems such as high cost and complicated process, and achieve the effects of uniform and complete reaction, good ductility, and large free volume
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Embodiment 1
[0037] This example aims to illustrate a method for preparing an ultra-high flux composite nanofiltration membrane, and the specific steps are as follows:
[0038] 1. Clean the base membrane: use polyethersulfone (PES) porous ultrafiltration membrane as the support layer, soak it in an aqueous solution containing 1% alcohol for 15 minutes, and clean it with an ultrasonic cleaner for one minute. Repeat the above steps twice to remove the ultrafiltration membrane Chemicals added during preparation and storage were cleaned and stored in a 4°C refrigerator for later use.
[0039] 2. Prepare composite aqueous monomer solution: use pure water as a solvent to configure an aqueous solution containing 0.1w / v% piperazine, 1w / v% hyperbranched polyester molecules, and 0.4w / v% sodium hydroxide, and stir fully After dissolving, store in an incubator at 25°C for future use.
[0040] 3. Prepare the organic phase monomer solution: use n-hexane as the organic solvent to prepare an organic phase ...
experiment example 1
[0043] The ultra-high flux composite nanofiltration membrane prepared in Example 1 is tested for performance:
[0044] Through the cross-flow filtration device, the performance test of pure water flux and salt rejection rate was carried out under the conditions of operating pressure 2bar and temperature 25°C. Using 1000ppm sodium sulfate salt solution as the feed liquid, the feed salt solution and filter salt were measured by conductivity meter Conductivity of the solution and calculate the cutoff. Measurement results: the flux of pure water is 51.62L / (m2·h·bar), and the rejection rate of sodium sulfate is 98.01%.
[0045] The measurement results were compared with the performance of the prepared nanofiltration membranes in the actual cases disclosed in some invention patents (or patent applications), as shown in Table 1.
[0046] Table 1
[0047]
[0048] Can find out by above comparison, under the premise of keeping the high rejection rate to sodium sulfate, the pure wa...
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