Regeneration method of performance of immersion-type ultrafiltration membrane used in reclaimed water recycling
A submerged, ultrafiltration membrane technology, applied in the direction of ultrafiltration, chemical instruments and methods, membrane technology, etc., can solve the problems of not meeting the water consumption requirements, water flux reduction, pressure difference increase, etc., to prolong the service life , recovery performance, and the effect of ensuring water volume
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Embodiment 1
[0062] The reclaimed water advanced treatment station of Taiyuan Iron and Steel Energy Power Plant uses reclaimed water as the water source, and adopts double membrane method for deep desalination. The water produced reaches the standard of desalinated water, and the conductivity is below 70 us / cm. It is used as high-quality stainless steel for the production of stainless steel. water. In this technology, the ultrafiltration adopts CS submerged ultrafiltration from Memcor, Australia. The membrane filament is a hollow fiber membrane. The ultrafiltration membrane pool adopts a concrete structure. It has the characteristics of low cost, corrosion resistance, solidity and non-deformation. After being put into operation in 2009, after years of practice, a method suitable for the performance regeneration of the submerged ultrafiltration membrane in the reuse of water was found.
[0063] After the membrane has been running for 30 minutes, the measured permeable pressure difference is 20...
Embodiment 2
[0068] Method of performance regeneration of submerged ultrafiltration membrane in reclaimed water reuse:
[0069] During the operation of the membrane, when the operation time is 20 minutes, when the transmembrane pressure difference suddenly reaches 25 kPa, the physical regeneration method is directly adopted, and the specific implementation method is the same as in Example 1.
Embodiment 3
[0071] Method of performance regeneration of submerged ultrafiltration membrane in reclaimed water reuse:
[0072] During the operation of the membrane, the running time is 85 hours and the transmembrane pressure difference suddenly reaches 80 kPa, and the short-period and short-time chemical cleaning method is directly adopted. The specific implementation method is the same as that in Example 1.
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