Antibacterial polyolefin microfiltration membrane and preparation method thereof
A polyolefin and microfiltration membrane technology, which is applied in the field of membrane separation, can solve the problems that the antibacterial effect of polyolefin microfiltration membrane cannot be maintained for a long time, and the antibacterial effect is poor.
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Embodiment 1
[0100] 1) Add ultra-high molecular weight polyethylene L5000 type (Mitsui Corporation of Japan), DCOIT (Shijiazhuang Boya Xinyi Technology Co., Ltd.), DCP (Sunshine International Industry Group Co., Ltd.) to 300# liquid paraffin (Tianjin Fuyu Fine Chemical Co., Ltd. company) and mixed evenly, put it into a twin-screw extruder and extrude at 200°C, and keep a vacuum of -0.09MPa during extrusion; wherein: every 100 parts by weight of the casting solution contains ultra-high molecular weight polyethylene. 20 parts by weight, 0.5 parts by weight of DCOIT, 0.1 parts by weight of DCP, and 79.4 parts by weight of liquid paraffin.
[0101] 2) After the casting solution obtained in step (1) passes through a filter to remove impurities, it is sent into the outer cavity of the die head of the hollow fiber membrane by the extruder, and the core with a pressure of 0.1MPa is used to hydraulically inject the core with a temperature of 170°C into the cavity. In the inner cavity of the die for...
Embodiment 2
[0103] 1) Add polypropylene J1300 type (Beijing Yanshan Petrochemical Co., Ltd.), carbendazim (Ningbo Sinochem Chemical Co., Ltd.), BPO (Jiangsu Taizhou Yuanda Chemical Raw Materials Co., Ltd.) to castor oil (Xinji City Hongyun Vegetable Oil Factory) ) and mix and stir evenly, gradually raise the temperature to 220°C under the condition of nitrogen protection, continue to stir for 1 hour to obtain the casting solution, and then keep it warm for 1.5 hours for defoaming; wherein: per 100 parts by weight of the casting solution Contains 15 parts by weight of polypropylene, 1 part by weight of carbendazim, 0.2 parts by weight of BPO, and 83.8 parts by weight of castor oil.
[0104] 2) After filtering the casting solution prepared in step (1) to remove impurities, press nitrogen with a pressure of 0.14MPa into the outer cavity of the hollow fiber membrane, and use nitrogen with a pressure of 0.12MPa to pressurize the core at a temperature of 200°C. Hydraulic pressure is injected in...
Embodiment 3
[0106] 1) Ultra-high molecular weight polyethylene M II type (Beijing Auxiliary No. 2 Factory), chlorothalonil (Yunnan Chemical Plant), nano-zeolite zinc-loaded antibacterial agent (Haier Kehua Company), DCP (Sunshine International Industry Group Co., Ltd.) Add diphenyl ether (Alfa Aisha (Tianjin) Chemical Co., Ltd.) and mix evenly, put it into a twin-screw extruder to extrude at 210°C, and maintain a vacuum of -0.09MPa during extrusion; where: each 100 parts by weight of casting solution contains 25 parts by weight of ultra-high molecular weight polyethylene, 5 parts by weight of chlorothalonil, 1 part by weight of nano-zeolite zinc-loaded antibacterial agent, 0.5 parts by weight of DCP, and 68.5 parts by weight of diphenyl ether.
[0107] 2) After the casting solution obtained in step (1) passes through the filter to remove impurities, it is sent into the salivating film die by the extruder. The temperature of the die is 210°C. It is shaped into a hollow fiber membrane in a ...
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