Cleaning method of immersed ultrafiltration membrane
An ultrafiltration membrane and submerged technology, which is applied in the cleaning field of submerged ultrafiltration membranes, can solve the problems of decreased permeate flux, increased transmembrane pressure difference, and difficulty in cleaning, etc., to reduce operating pressure and reduce transmembrane The effect of pressure difference and restoration of permeate flux
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Embodiment 1
[0022] Embodiment one: the concrete cleaning step to submerged ultrafiltration membrane is:
[0023] 1) The first alkaline cleaning: empty the ultrafiltration membrane pool, transport the alkaline cleaning solution into the ultrafiltration membrane pool, until the cleaning solution completely submerges the ultrafiltration membrane wire, soak the ultrafiltration membrane for 8 hours, soak During the process, use compressed air or Roots blower to aerate and stir the soaking liquid and ultrafiltration membrane filaments in the ultrafiltration membrane pool, and aerate for 1min every 1h. Alkaline cleaning solution is prepared with reverse osmosis water or low hardness tap water, the temperature is 25°C, the composition is sodium hydroxide and sodium hypochlorite, the mass fraction of sodium hydroxide is 2%, the concentration of sodium hypochlorite is 4000ppm in terms of available chlorine, and the rest is reverse osmosis Produced water or tap water with low hardness;
[0024] 2) ...
Embodiment 2
[0031] Embodiment 2: The specific operation steps are the same as in Embodiment 1, and the citric acid in step 3 is replaced with oxalic acid prepared with a mass concentration of 2%.
[0032] The test results of the embodiment of the present invention: after cleaning, the transmembrane pressure difference was restored from -70kPa to -10kPa during the operation of the ultrafiltration membrane, the permeate flux was 100% restored to the design flux, and the cleaning period was extended to 30 days.
[0033] The pollutants cannot be thoroughly cleaned by other cleaning methods, and the transmembrane pressure difference can only be restored to -35kPa, and the permeate flux can only be restored to 50% of the design flux, and the transmembrane pressure difference is restored rapidly after 4 days increased to -70kPa.
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