Hollow fiber ultrafiltration membrane of polysulfone with permanent hydrophilicity and its preparing process
An ultrafiltration membrane, hydrophilic technology, applied in the field of polymer membrane and its manufacturing, can solve the problem of not seeing, and achieve the effect of shortening the reaction time
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Embodiment 1
[0010] In the ordinary spinning solution composed of 18% polysulfone (domestic or BASF production, intrinsic viscosity 0.58 ~ 0.6), 10% polyethylene glycol (PEG400) and 72% dimethylformamide, add 4% K-15 / K-30 in a ratio of 2:1, under normal operating conditions, used for wet spinning to obtain a hollow fiber membrane with an inner diameter of 0.9 mm and a wall thickness of 0.25 mm. , take it out after washing for 4 hours, control the moisture and place it in a tubular high-pressure reactor, which contains 0.1% concentration of K 2 S 2 o 8 solution, heating the reactor so that the water temperature quickly reaches 110°C, and then cooling down after 20 minutes of heat preservation. After the water temperature drops below 50°C, open the reactor to take out the fiber filaments, dry them in an oven at 105°C for 8 hours. Direct rehydration, the pure water flux measured at a membrane penetration pressure of 0.1MPa is 250l / m 2 .h.
Embodiment 2
[0012] Change the polysulfone content from 18% to 16% in the spinning solution, the ratio of K-15 / K-30 is from 2:1 to 1:3, and the rest are the same as in Example 1. After the dry membrane is directly rehydrated, it is measured that the pure water flux is 310l / m at a membrane penetration pressure of 0.1MPa 2 h.
Embodiment 3
[0014] The percentage by weight of the mixture of K-15 / K-30 added in the spinning solution is increased from 4% to 6%, and the ratio of K-15 / K-30 is changed from 2:1 to 3:1, and the others are the same Example 1. After the dry membrane is directly rehydrated, it is measured that the pure water flux is 200l / m at a membrane penetration pressure of 0.1MPa 2 .h.
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