Polyvinylidene fluoride hollow fiber membrane and preparation method thereof
The technology of polyvinylidene fluoride and polyvinylidene fluoride resin is applied in the field of polyvinylidene fluoride hollow fiber membrane and its preparation, which can solve the problems of long production cycle, many defects of pores in membrane fibers, and reduced water flux, etc. , to achieve the effect of reducing production costs, optimizing large-scale production processes, and facilitating production arrangements
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Embodiment 1
[0034] The weight-average molecular weight is 300,000 polyvinylidene fluoride mixed with butyl benzoate and calcium carbonate, wherein the content of polyvinylidene fluoride is 55wt%, the content of calcium carbonate is 32wt%, and the content of butyl benzoate is 13wt%, The above three materials are mixed by a high-speed mixer, and the materials are heated and melted at 180°C by a twin-screw extruder, meshed and modified, extruded by a granulation die, cooled and formed into pellets, and stored in bags as semi-finished products .
[0035]The obtained pellets are melted at 200°C, pressurized by the melt pump to 15MPa, extruded through the circular ring mouth of the extruder, and the extrusion stretching ratio is controlled to be 9, and the extruded product is immersed in 35°C Stretching was carried out in a water bath with a stretching rate of 15 m / min and a stretching ratio of 4. Then heat-setting treatment is carried out for about 30 seconds, and the temperature is controlle...
Embodiment 2
[0038] Mix polyvinylidene fluoride with a weight average molecular weight of 350,000, acetyl tributyl citrate and calcium carbonate, wherein the content of polyvinylidene fluoride is 50wt%, the content of calcium carbonate is 35wt%, and the content of acetyl tributyl citrate The content is 15wt%. The above three materials are mixed by a high-speed mixer, and the materials are heated and melted at 220°C with a twin-screw extruder, and the meshing is modified. Bags are stored as semi-finished products.
[0039] The obtained pellets are melted at 240°C, pressurized by a metering pump to 12MPa, extruded through the ring die of the extruder, and the extrusion stretch ratio is controlled to be 8, and the extruded product is immersed in a water bath at 25°C Stretching was carried out in , the stretching rate was 10m / min, and the stretching ratio was 6. Then annealing heat setting treatment is carried out for 15 seconds, and the temperature is controlled at 120° C. to obtain a hollow...
Embodiment 3
[0042] Mix polyvinylidene fluoride with a weight-average molecular weight of 320,000, phthalate, and silicon dioxide, wherein the content of polyvinylidene fluoride is 55 wt%, the content of silicon dioxide is 30 wt%, and phthalic acid The content of the ester is 15wt%. The above three materials are mixed by a high-speed mixer, and the materials are heated and melted at 200°C with a twin-screw extruder, and the meshing is modified. Granules, bagged and stored as semi-finished products.
[0043] The obtained pellets are melted at 230°C, pressurized to 10MPa by a melt pump, extruded through the circular ring of the extruder, and the extrusion stretching ratio is controlled to be 8, and the extruded product is immersed in a 30°C Stretching was carried out in a water bath with a stretching rate of 15 m / min and a stretching ratio of 5. Then carry out annealing and thermal setting treatment for about 80 seconds, and the temperature is controlled at 150° C., so that the hollow fiber...
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