A method for biological denitrification of domestic sewage and a method for starting the system
A domestic sewage and biological denitrification technology, applied in biological water/sewage treatment, chemical instruments and methods, water/sludge/sewage treatment, etc., can solve problems such as unrealizable, difficult to stabilize nitrosation process, low ammonia nitrogen concentration, etc. , to achieve the effects of easy upgrading, excellent denitrification effect and low operating cost
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specific Embodiment approach 1
[0019] Specific embodiment 1: The biological denitrification method of domestic sewage in this embodiment: the domestic sewage is passed into the activated domestic sewage biological denitrification treatment system for denitrification treatment; DO (dissolved oxygen) control during the operation of denitrification treatment is less than 0.5mg / L.
[0020] The biological denitrification treatment system for domestic sewage in this embodiment 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 for oxygen, It is more inclined to accumulate in the outer layer of the sludge to obtain oxygen, and after the consumption of the surface AOB, the inner layer of the sludge is an anaerobi...
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 2-6 hours. Other steps and parameters are the same as in the first embodiment.
specific Embodiment approach 3
[0022] Specific embodiment three: the starting method of the domestic sewage biological denitrification treatment system in this embodiment:
[0023] 1. Place the denitrified granular sludge in the reaction zone of the EGSB reactor, and the pH value is 7.8-8.0, the temperature is 30±2℃, and the NLR is 0.24kgN (m 3 d)±0.01kgN(m 3 d) artificial inflow operation, DO (dissolved oxygen) is controlled to <0.3mg / L during the operation, and NLR (nitrogen volume load rate) is gradually increased 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 ≥0.88, the ratio of nitrate nitrogen production / ammonia nitrogen removal ≤0.11, and the relative abundance of NOB <1%;
[0024] 2. The pH value is 7.8~8.0 and the NLR is 0.24kgN (m2) into the EGSB reactor 3 d)±0.01kgN(m 3 d) Simulated sewage operation, DO control <0.3mg / L during operation, if nit...
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