Breathable and hydrophobic mixed matrix membrane and preparation method thereof
A mixed-matrix membrane, hydrophobic technology, applied in semi-permeable membrane separation, chemical instruments and methods, membranes, etc., can solve the problems such as literature reports on porous carbon microspheres that have not been found, and achieve good modifiability, improved anti-pollution performance, The effect of reducing the phenomenon of agglomeration
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Embodiment 1
[0039] Preparation method of fluoroalkylation modified porous carbon microspheres:
[0040] ⑴ Dissolve 1.0g of porous carbon microspheres in a mixed acid consisting of 75ml of concentrated sulfuric acid and 25ml of concentrated nitric acid, heat and stir at 80°C, and 50Hz ultrasonic treatment to graft hydroxyl and carboxyl functional groups on the surface of porous carbon microspheres to obtain carboxylated Porous carbon microspheres;
[0041] (2) The carboxylated porous carbon microspheres were dissolved in 20ml of hexafluoroisopropanol, heated at 90°C and stirred, and catalyzed by concentrated sulfuric acid to obtain fluoroalkylated modified porous carbon microspheres.
Embodiment 2
[0043] Preparation of flat membrane:
[0044] Weigh 30g of PVDF powder, 120ml of solvent DMAc, 20ml of porogen, and 0.3g of fluoroalkylated modified porous carbon microspheres. Stir fully and dissolve at 75°C to keep the solution uniform and stable. Keep the temperature constant, stop stirring, stand for 12 hours to degas, and scrape a flat film on a flat glass plate.
[0045] Table 1 Performance data statistics of the prepared mixed matrix flat membrane
[0046]
Embodiment 3
[0048] Preparation of hollow fiber membrane:
[0049] Weigh 30 g of PVDF powder, 120 ml of solvent DMAc, 20 ml of porogen, and 0.3 g of fluoroalkylated modified porous carbon microspheres. Stir and dissolve at 75° C. to keep the solution uniform and stable. Keep the temperature constant, stop stirring, stand for 12 hours to degas and spin to prepare hollow fiber membranes. The main component of the coagulation bath liquid is water, and the spinning draft speed is 25 m / min. The core of the spinning nozzle is inserted into the tube to pass the core liquid. The obtained polyvinylidene fluoride hollow fiber separation membrane has an inner diameter of 800 μm and a fiber wall thickness of 200 μm. The membrane is distilled Flux 39.3kg / m 2 h.
[0050] Table 2 Performance data statistics of the prepared mixed matrix hollow fiber membranes
[0051]
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