Multipoint water-in sludge in-situ reduction synchronous coupling nitrogen and phosphorus removal method
A synchronous coupling, denitrification and dephosphorization technology, applied in the direction of water/sludge/sewage treatment, water pollutants, biological sludge treatment, etc., can solve the problem that sludge cannot be reduced in situ, so as to reduce infrastructure investment and improve Effect of Nitrogen and Phosphorus Removal Efficiency
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Embodiment 1
[0022] Step 1, the raw sewage enters the anaerobic pool 2 and the anoxic pool 3 according to the volume distribution ratio of 5:5, and the raw sewage CODCr concentration, TN concentration, NH3-N concentration, TP concentration, water temperature, anaerobic pool 2 and anoxic pool The HRT of Pool 3 was determined to be 396mg / L, 36mg / L, 34mg / L, 3mg / L, 28°C, 1.89h, and 0.94h, respectively;
[0023] Step 2, the aerobic pool 4 receives the mud-water mixture discharged from the anaerobic pool 2 and the anoxic pool 3, and the HRT, DO concentration and temperature of the aerobic pool 4 are respectively determined to be 1.85h, 2mg / L and 28°C;
[0024] Step 3, the mud-water mixture discharged from the aerobic tank 4 enters the sedimentation tank 5 and the anoxic tank 3 respectively according to the volume distribution ratio of 1:2.5, and the sedimentation time of the sedimentation tank 5 is determined to be 1 hour;
[0025] Step 4: After the mud-water separation is carried out in the sed...
Embodiment 2
[0029] Step 1, the raw sewage enters the anaerobic pool 2 and the anoxic pool 3 according to the volume distribution ratio of 5:5, and the raw sewage CODCr concentration, TN concentration, NH3-N concentration, TP concentration, water temperature, anaerobic pool 2 and anoxic pool The HRT of Pool 3 was determined to be 512mg / L, 64mg / L, 52mg / L, 9mg / L, 28°C, 1.89h, and 0.94h, respectively;
[0030] Step 2, the aerobic pool 4 receives the mud-water mixture discharged from the anaerobic pool 2 and the anoxic pool 3, and the HRT, DO concentration and temperature of the aerobic pool 4 are respectively determined to be 1.85h, 2mg / L and 28°C;
[0031] Step 3, the mud-water mixture discharged from the aerobic tank 4 enters the sedimentation tank 5 and the anoxic tank 3 respectively according to the volume distribution ratio of 1:2.5, and the sedimentation time of the sedimentation tank 5 is determined to be 1 hour;
[0032] Step 4: After the mud-water separation is carried out in the sed...
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