Porous hollow fibre membrane, its manufacturing method and use, porous hollow fibre membrane block and its use
A manufacturing method and porous technology, which can be used in hollow filament manufacturing, rayon manufacturing, chemical instruments and methods, etc., can solve the problems of inability to improve water quality, low proportion of hollow fiber membrane filtration, and increased equipment costs.
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Embodiment 1
[0085] Manufactured in the following order, from polysulfone (UDEL-P1800, Amoco Japan Co., Ltd. PSF) 20% by weight, ethylene glycol (EG) 6% by weight, silicon oxide (average particle size 4.5μm) 18% by weight and A spinning dope composed of 54% by weight of N,N-dimethylacetamide (DMAc). That is, after dissolving ethylene glycol in N,N-dimethylacetamide, use a homogenizer to uniformly disperse silicon oxide powder in N,N-dimethylacetamide, and add Polysulfone was added, followed by stirring at 60° C. for 8 hours to dissolve the polysulfone and obtain a white slurry-like spinning dope in which silicon oxide was uniformly dispersed.
[0086] After degassing the spinning dope obtained by the above method, keep it at 50°C, and mix it with N,N-dimethylformamide ( An injection solution consisting of 80% by weight of DMF, 19% by weight of water, and 1% by weight of polyvinyl alcohol (PVA205, manufactured by Kuraray Co., Ltd., PVA) was sprayed together. This was run for 10 cm in a 50...
Embodiment 2
[0090] Except that the spinning dope is made of 20% by weight of polysulfone, 6% by weight of ethylene glycol, 20% by weight of silicon oxide (average particle size 11 μm), 2% by weight of silicon oxide (average particle size 4.5 μm), 52% by weight A hollow fiber membrane was obtained in the same manner as in Example 1 except that % N,N-dimethylacetamide was constituted. The resulting hollow fiber membrane has a pure water permeation rate of 520,000L / m 2 / hr / 100kPa, classified particle size is 5.0μm.
Embodiment 3
[0092] Except that the spinning dope is composed of 20% by weight of polysulfone, 4% by weight of ethylene glycol, 14% by weight of silicon oxide (average particle size 1.5 μm), and 62% by weight of N,N-dimethylformamide , and other hollow fiber membranes were obtained in the same manner as in Example 1. The resulting hollow fiber membrane has a pure water permeation rate of 39000L / m 2 / hr / 100kPa, classified particle size is 1.2μm.
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