Method for advanced treatment of ammonia nitrogen sewage
A technology for advanced treatment and sewage, applied in the field of advanced treatment of ammonia nitrogen sewage, can solve problems such as no public reports and inability to discharge sewage up to standard, and achieve the effect of improving treatment capacity and improving capacity.
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Embodiment 1
[0035] a. Ammonia nitrogen sewage is collected into the regulating pool, and multiple submersible push-flow mixers are installed in the regulating pool. The hydraulic retention time of the sewage in the regulating pool is 8 hours, which plays a good role in regulating the water quality and quantity of the sewage;
[0036] b. Then use the submersible sewage pump to lift the sewage to the biochemical pool. The biochemical pool is divided into an anaerobic pool with added biochemical plates, partition walls and biochemical balls and an aerobic pool with biochemical balls added. Microbial preparations are added to the aerobic pool (addition amount 0.3kg / 10000m 3 ), degrade COD, BOD, NH in sewage 3 -N and other pollutants; add microbial preparations in the anaerobic pool (addition amount 0.2kg / 10000m 3 ) and carbon source methanol (addition amount 100kg / 10000m 3 ) for denitrification, the addition of microbial preparations and carbon source methanol is based on NH 3 -N, dependin...
Embodiment 2
[0041] Basically with embodiment 1. The difference is: adding microbial preparations in the aerobic pool (addition amount 0.4kg / 10000m 3 ), degrade COD, BOD, NH in sewage 3 -N and other pollutants; add microbial preparations in the anaerobic pool (addition amount 0.3kg / 10000m 3 ) and no carbon source methanol was added to the denitrification anaerobic tank without adding carbon source methanol.
[0042] Example 2:
[0043] Basically with embodiment 1. The difference is: add microbial preparations in the aerobic pool (addition amount 0.5kg / 10000m 3 ), degrade COD, BOD, NH in sewage 3 -N and other pollutants; add microbial preparations in the anaerobic pool (addition amount 0.4kg / 10000m 3 ) and carbon source methanol (added amount 50kg / 10000m 3 ) does not add carbon source methanol to the denitrification anaerobic tank.
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