Efficient nitrogen and phosphorus removal township sewage treatment method and device
A sewage treatment method and sewage treatment device technology, applied in the directions of water/sewage multi-stage treatment, biological water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problem of poor nitrogen and phosphorus removal and unstable operation , strict nitrogen and phosphorus emission standards, etc., to achieve the effect of improving oxygen transfer efficiency, good removal effect, and reducing load
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[0031] Example 1
[0032] A method and device for high-efficiency denitrification and dephosphorization of village and town sewage treatment, including a sludge tank (8) and a pre-denitrification tank (1), anaerobic tank (2), and aerobic tank (3) connected in sequence , Anoxic tank (4), aerobic tank 2 (5), MBR tank (6) and disinfection and clean tank (7), which include the following steps:
[0033] 1) Village and town sewage influent is divided into two parts, 70% enters the pre-denitrification tank (1), mixed with the sludge returned from the MBR tank (6), and the reaction time is 1 hour; 30% of the influent enters the anoxic tank ( 4).
[0034] 2) After the pre-denitrification treatment, the sewage enters the anaerobic tank (2) for anaerobic phosphorus release reaction, creating favorable conditions for the removal of total phosphorus in the aerobic stage, the residence time is 1 hour, and the subsequent aerobic tank 1 The pond (3) forms an A / O treatment process, so as to achieve...
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[0040] Example 2
[0041] 1) Village and town sewage influent is divided into two parts, 70% enters the pre-denitrification tank (1), mixed with the sludge returned from the MBR tank (6), and the reaction time is 1 hour; 30% of the influent enters the anoxic tank ( 4).
[0042] 2) After the pre-denitrification treatment, the sewage enters the anaerobic tank (2) for anaerobic phosphorus release reaction, creating favorable conditions for the removal of total phosphorus in the aerobic stage, and the residence time is 1 hour.
[0043] 3) After the sewage passes through the anaerobic tank (2), it enters the aerobic tank 1 (3). When the aerobic tank 1 (3) is not aerated, it becomes an anoxic tank. The reaction time is 2-3 hours. The subsequent anoxic pools (4) constitute the operation mode of the anoxic pools at both ends to strengthen the removal of nitrogen.
[0044] 4) After the sewage passes through the aerobic tank 1 (3), it enters the anoxic tank (4), and mixes with the 30% influent...
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