Distributed sewage treatment system and treatment method using the treatment system
A treatment system, decentralized technology, applied in the field of decentralized sewage treatment system, to achieve the effect of reducing organic matter load and pollution
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Embodiment 2
[0131] The wastewater to be treated is a point source sewage outlet by a river, mainly domestic sewage including some industrial wastewater. The main feature is that the water quality fluctuates greatly. The main pollutant indicators are: COD is 432.5~551.3mg / L, BOD 5 SS is 168.5-236.4mg / L, SS is 151.3-248.5mg / L, total nitrogen is 51.5-90.1mg / L, ammonia nitrogen is 38.9-63.1mg / L, and total phosphorus is 8.6-15.9mg / L.
[0132] Put the domestic wastewater into the regulating tank of the integrated treatment equipment, enter the primary sedimentation tank through the regulating tank, stay for 0.5~1h to remove SS, discharge the sludge from the primary sedimentation tank to the sludge concentration tank every 2~4h, and enter the supernatant The anaerobic tank stays for 1-2 hours for anaerobic phosphorus release, enters the anoxic tank for 1-2 hours for denitrification, and enters the aerobic tank for 6-10 hours to complete the removal of COD, ammonia nitrogen and total phosphorus. P...
Embodiment 3
[0136] The wastewater to be treated is the sewage outlet of a small enterprise. It is mainly domestic sewage including some industrial wastewater. The main feature is high ammonia nitrogen content. The main pollutant indicators are: COD is 312.1~392.3mg / L, BOD 5 SS is 139.8-156.4mg / L, SS is 93.4-105.1mg / L, total nitrogen is 114.6-136.5mg / L, ammonia nitrogen is 89.4-101.4mg / L, and total phosphorus is 7.9-10.2mg / L.
[0137] Put the domestic wastewater into the regulating tank of the integrated treatment equipment, enter the primary sedimentation tank through the regulating tank, stay for 0.5h to remove SS, discharge the sludge from the primary sedimentation tank to the sludge concentration tank every 6 hours, and the supernatant enters the anaerobic tank , stay 0.75h for anaerobic phosphorus release, enter the anoxic pool for 1.25h for denitrification, enter the aerobic pool for 8-10h oxidation to complete the removal of COD, ammonia nitrogen and total phosphorus, part of the eff...
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