Porous film and method for preparation thereof
A porous membrane and resin technology, applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problems of unfavorable cost and complicated process
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Embodiment 1
[0066] 6 parts by weight of organic clay (SPN manufactured by Copp Chemical Co., Ltd.) obtained by organicizing inorganic phyllosilicate with an alkylene oxide compound was added to 64 parts by weight of diethyl phthalate, and ultrasonic waves were applied. While stirring with a stirring blade at a speed of 3000 rpm at room temperature for 4 hours, it was dispersed. Next, 30 parts by weight of polyvinylidene fluoride (manufactured by Solbey Co., Ltd., SOLEF6020) was added, and kneaded at 180° C. at a rotation speed of 50 rpm for 15 minutes. After kneading, it is cooled to room temperature to make a film-making stock solution. Next, heat the prepared film-making stock solution to 180°C to melt it evenly again, press it into a flat film with a thickness of 200 μm, and then put it into a water bath at 5°C for cooling to make a porous film. plasma membrane. The average pore diameter of this porous membrane was 0.1 μm, and the porosity was 64%.
Embodiment 2
[0068]The mixing ratio of the film-making stock solution was adjusted to 2 parts by weight of organic clay, 58 parts by weight of diethyl phthalate, and 40 parts by weight of polyvinylidene fluoride, except that the same operation as in Example 1 was carried out to prepare Porous membrane. The average pore diameter of this porous membrane was 0.1 μm, and the porosity was 65%.
Embodiment 3
[0074] 1.5 parts by weight of organic clay (SPN manufactured by Copp Chemical Co., Ltd.) obtained by organicizing inorganic layered silicate with an alkylene oxide compound, 68.5 parts by weight of diethyl phthalate, and 30 parts by weight of polyvinylidene fluoride Parts were mixed according to the method in Example 1 to obtain a membrane-forming stock solution. Raise the temperature of the film-making stock solution to 180°C again, use diethyl phthalate at 180°C as the core liquid, and extrude it through a double ring die at an extrusion speed of 0.2m / min until the temperature is adjusted to 5°C A hollow porous membrane having an outer diameter of 1.0 mm and an inner diameter of 0.7 mm was obtained in a cooling water tank. The height from the die to the cooling water tank is 2 cm. The average pore diameter of this porous membrane was 0.1 μm, and the porosity was 65%.
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