Method of inhibiting membrane contamination of membrane bioreactor
A technology of membrane bioreactor and membrane inhibition, applied in chemical instruments and methods, biological water/sewage treatment, sustainable biological treatment, etc., to avoid trouble and secondary pollution, have sufficient theoretical basis, and inhibit membrane fouling
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Embodiment 1
[0012] Inoculation of aerobic flocculent activated sludge. Membrane bioreactor feed water is simulated domestic sewage, and the water quality is as follows: COD concentration is 200mg / L, ammonia nitrogen is 15mg / L, pH value is 6.8, dissolved oxygen concentration is 2.0mg / L, hydraulic retention time is 4h, sludge retention time for 5 days. When it runs to about 30 days, it can be found that there is aerobic granular sludge in the membrane bioreactor by visual inspection. Under the same experimental conditions as the control example, the membrane flux is 15-20L / m 2 h.
Embodiment 2
[0014] Inoculation of aerobic flocculent activated sludge. Membrane bioreactor feed water is simulated domestic sewage, and the water quality is as follows: COD concentration is 500mg / L, ammonia nitrogen is 50mg / L, pH value is 7.5, dissolved oxygen concentration is 4.0mg / L, hydraulic retention time is 7h, sludge retention time for 7 days. When it runs to about 25 days, it can be observed with the naked eye that there is aerobic granular sludge in the membrane bioreactor. Under the same experimental conditions as the control example, the membrane flux is 15-20L / m 2 h.
Embodiment 3
[0016] Inoculation with aerobic granular sludge. Membrane bioreactor feed water is simulated domestic sewage, and the water quality is as follows: COD concentration is 1000mg / L, ammonia nitrogen is 100mg / L, pH value is 8.0, dissolved oxygen concentration is 6.0mg / L, hydraulic retention time is 10h, sludge retention time for 10 days. The physical and chemical properties of aerobic granular sludge can be maintained in membrane bioreactors. Under the same experimental conditions as the control example, the membrane flux is 15-20L / m 2 h.
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