Polymer membrane for mixing and ultrafilter and its preparing process
A technology of ultrafiltration membranes and polymers, applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problems of difficult use, whitening, and limited membranes, and achieve the effect of improving anti-pollution
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Embodiment 1
[0055] 2.5 grams of chloromethylated polysulfone and 7.5 grams of polyvinylidene fluoride were dissolved in 88 ml of dimethyl sulfoxide, and the chloromethyl content of the chloromethylated polysulfone was 2.2 mol / kg (meq / g); After the polymer is completely dissolved, it is filtered and left standing for defoaming. Using ultrafiltration water as the coagulation medium, the ultrafiltration membrane is prepared by the phase inversion method, and the thickness of the membrane is about 200 μm. The membrane has an operating pressure of 0.1MPa and a pure water flux of 445.6L / m 2 h, the rejection rate of 0.1 g / L bovine serum albumin aqueous solution is 82.7%.
Embodiment 2
[0057] 4 grams of chloromethylated polysulfone and 8 grams of polyvinylidene fluoride were dissolved in 86 ml of dimethyl sulfoxide, and the chloromethyl content of the chloromethylated polysulfone was 2.2 mol / kg (meq / g); After the polymer is completely dissolved, add 3 grams of polyethylene glycol 600. After the dissolution is uniform, filter and stand for defoaming, use ultrafiltered water as the coagulation medium, and the temperature of the coagulation medium is 10°C. Filter membrane with a thickness of about 200 μm. The membrane has an operating pressure of 0.1MPa and a pure water flux of 380.2L / m 2 h, the rejection rate of 0.1 g / L bovine serum albumin aqueous solution is 65.4%.
Embodiment 3
[0059] Dissolve 2.5 grams of chloromethylated polysulfone and 10 grams of polyvinylidene fluoride in 88 milliliters of dimethyl sulfoxide, and the chloromethyl content of the chloromethylated polysulfone is 2.2 mol / kg (meq / g); After the polymer is completely dissolved, it is filtered and left standing for defoaming. Using ultrafiltration water as the coagulation medium, the ultrafiltration membrane is prepared by the phase inversion method, and the thickness of the membrane is about 200 μm. The membrane has an operating pressure of 0.1MPa and a pure water flux of 144.4L / m 2 h, the rejection rate of 0.1 g / L bovine serum albumin aqueous solution is 86.1%, and the pure water flux attenuation coefficient m 1 It is 16.8; the pure water flux recovery coefficient of cathodic electrophoretic paint is 204.5.
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