Vinylidene fluoride resin hollow filament porous membrane, water filtration method using the same, and process for producing said vinylidene fluoride resin hollow filament porous membrane
A technology of ethylene difluoride and porous membrane, which is applied in the field of 1, and can solve the problem that the hollow fiber porous membrane has not been developed.
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Embodiment 1
[0101] The weight average molecular weight (Mw) is 4.12×10 5 The main body of polyvinyl difluoride (PVDF) (powder) with Mw is 9.36×10 5 Polyvinylidene fluoride (PVDF) (powder) is used for the modification of the crystallization characteristics of 95% by weight and 5% by weight respectively, and is mixed with a Henschel mixer to obtain a Mw of 4.38×10 5 Mixture A.
[0102] An adipic acid-based polyester plasticizer ("PN-150" manufactured by Asahi Denka Co., Ltd.) as an aliphatic polyester and N-methylpyrrolidone (NMP) as a solvent were mixed at 82.5% by weight / 17.5 The ratio of % by weight was stirred and mixed at room temperature to obtain a mixture B.
[0103] Using a co-rotating intermeshing twin-screw extruder ("BT-30" manufactured by Plastic Engineering Research Institute, screw diameter 30mm, L / D=48), the powder is supplied from the position 80mm from the most upstream part of the cylinder. Mixture A was supplied from the upper part, and mixture B heated to a temperatu...
Embodiment 2
[0110] The main body PVDF and the modified PVDF were mixed at a ratio of 90% by weight and 10% by weight respectively to obtain a Mw of 4.64×10 5 Mixture A.
[0111] Using this mixture A, increase the discharge rate from the nozzle of the molten mixture of mixture A and mixture B to 13.6 g / min, increase the flow rate of air supplied to the center of the nozzle to 4.8 ml / min, and then melt extrude into Hollow fiber, introduced into a cooling bath at 10°C, allowed to cool and solidify to obtain the first intermediate molded body, except that the draw ratio of the second intermediate molded body was changed to 1.8 times, and the other operations were the same as in Example 1. , to obtain a hollow fiber porous membrane.
Embodiment 3
[0113] In addition to using the main body PVDF and PVDF for modification, they were mixed at a ratio of 85% by weight and 15% by weight, and the Mw was 4.91×10 5 Except for the mixture A, the others were the same as in Example 2 to obtain a hollow fiber porous membrane.
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