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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Embodiment 1
[0032] A village and town sewage treatment method and device for efficient nitrogen and phosphorus removal, comprising a sludge tank (8) and sequentially connected pre-denitrification tank (1), anaerobic tank (2), and aerobic tank 1 (3) , anoxic pool (4), aerobic pool 2 pools (5), MBR pool (6) and disinfection and clear water pool (7), it comprises the following steps:
[0033] 1) The influent of village and town sewage is divided into two parts, 70% of which enters the pre-denitrification tank (1), and reacts with the sludge returned by 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 pool (3) forms an A / O method treatment process, so as...
Embodiment 2
[0041] 1) The influent of village and town sewage is divided into two parts, 70% of which enters the pre-denitrification tank (1), and reacts with the sludge returned by 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 pool (2), it enters the aerobic pool 1 (3). When the aerobic pool 1 (3) is not aerated, it becomes an anoxic pool, and the reaction time is 2-3 hours. The subsequent anoxic pool (4) constitutes the operation mode of the two-end anoxic pool to strengthen the removal of nitrogen.
[0044] 4) After the sewage passes through the aerobic pool 1 (3), it enters the anoxic pool (4), and reacts with 30% of th...
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