Domestic sewage biological denitrification method and system starting method
A technology for domestic sewage and biological denitrification, applied in biological water/sewage treatment, chemical instruments and methods, water/sludge/sewage treatment, etc. and other problems, to achieve the effect of easy upgrading, excellent denitrification effect and low start-up cost
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specific Embodiment approach 1
[0019] Specific implementation mode 1: The biological denitrification method of domestic sewage in this embodiment: feed the domestic sewage into the activated domestic sewage biological denitrification treatment system for denitrification treatment; DO (dissolved oxygen) control <0.5mg during the denitrification treatment operation process / L.
[0020] In this embodiment, the domestic sewage biological denitrification treatment system selects a granular sludge expanded bed reactor for domestic sewage treatment. The granular sludge in the domestic sewage biological denitrification treatment system of this embodiment is enriched by AOB and AnAOB, wherein the outer layer of the granular sludge is AOB, and the inner layer of the granular sludge is AnAOB. Due to the higher affinity of AOB to oxygen, It tends to accumulate in the outer layer of sludge to obtain oxygen, and after the consumption of surface AOB, the inner layer of sludge is an anaerobic zone, which is suitable for ...
specific Embodiment approach 2
[0021] Embodiment 2: The difference between this embodiment and Embodiment 1 is that the hydraulic retention time of the denitrification treatment is 2 to 6 hours. Other steps and parameters are the same as those in Embodiment 1.
specific Embodiment approach 3
[0022] Specific implementation mode three: the start-up method of the domestic sewage biological denitrification treatment system in this implementation mode:
[0023] 1. Put the denitrification granular sludge in the reaction zone of the EGSB reactor. 3 d)±0.01kgN(m 3 d) artificial water intake operation, DO (dissolved oxygen) control <0.3mg / L during operation, gradually increase NLR (nitrogen volume loading rate) in stages; until the effluent ammonia nitrogen removal rate and total nitrogen removal rate reach 90% respectively And more than 80%, and the ratio of ammonia nitrogen removal / total nitrogen removal is ≥0.88, the ratio of nitrate nitrogen production / ammonia nitrogen removal is ≤0.11, and the relative abundance of NOB is less than 1%;
[0024] 2. Into the EGSB reactor, the pH value is 7.8-8.0, and the NLR is 0.24kgN (m 3 d)±0.01kgN(m 3 ·D) simulated sewage operation, DO control <0.3mg / L during operation, if the nitrate nitrogen production / ammonia nitrogen removal ...
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