Vinylidene fluoride resin porous film and manufacturing method therefor
A technology of ethylene difluoride and its manufacturing method, which is applied in the field of porous membranes and can solve problems such as excessively large average pore diameter of porous membranes and maintenance of water permeability
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Embodiment 1
[0123] Using a Henschel mixer, the weight average molecular weight (Mw) was 4.1×10 5 The substrate is polyvinyl difluoride (PVDF-I) (powder) and Mw is 9.7×10 5 Polyvinylidene fluoride (PVDF-II) (powder) for modifying the crystallization characteristics of the 1,1-difluoroethylene (PVDF-II) (powder) is mixed according to the ratio of 75% by weight and 25% by weight respectively, and the obtained Mw is 5.4×10 5 PVDF mixture (mixture A; crystallization temperature Tc after film formation = 150.4° C.).
[0124] As the plasticizer, adipic acid-based polyester-based plasticizer (polyester of adipic acid and 1,2-butanediol terminated with isononyl alcohol; "D623N" manufactured by Geeyi Plus Co., Ltd., number The average molecular weight is about 1800, and the measured viscosity at 25°C measured according to JIS K7117-2 (cone-plate rotary viscometer) is 3000mPa·s) and diisononyl adipate as a monomeric ester plasticizer Esters ("DINA" manufactured by Jiei Plus Co., Ltd.) were stirred...
Embodiment 2
[0132] The mixing ratio of PVDF-I and PVDF-II was changed to 95% by weight and 5% by weight respectively to obtain PVDF mixture A (crystallization temperature Tc = 148.8° C.), and the supply ratio of mixture A / mixture B was 33.9% by weight / 66.1 % by weight, and the temperature Tq of the cooling water bath was changed to 12° C., and the pulling speed was changed to 3.3 m / min. In the same manner as in Example 1, the polyvinylidene fluoride system of the present invention was obtained. Hollow fiber porous membrane.
Embodiment 3
[0134] The mixing ratios of the adipate-based polyester-based plasticizer "D623N" and the diisononyl adipate "DINA" were changed to 80% by weight and 20% by weight respectively to obtain a plasticizer mixture B, and the temperature of the cooling water bath was adjusted to The polyvinylidene fluoride-based hollow fiber porous membrane of the present invention was obtained in the same manner as in Example 2, except that Tq was changed to 85° C. and the pulling speed was changed to 4.3 m / min.
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