A method for further denitrification of high ammonia nitrogen wastewater based on the a/o process
A high-ammonia nitrogen and process technology, applied in chemical instruments and methods, biological water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of denitrification rate limitation, secondary pollution of effluent, and low denitrification rate. , to achieve the effect of easy industrialization, wide application range and high denitrification rate
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Embodiment 1
[0027] The invention is used to transform and upgrade the denitrification project of treating high-ammonia-nitrogen wastewater by the A / O process. Wastewater treatment capacity 1000m 3 d -1 , waste water COD2500mg·L -1 , TN450mg·L -1 , NH 3 -N350mg·L -1 . The original treatment process is A / O process, and the effective volume of A pool is 1600m 3 , the effective volume of O pool is 3400m 3 , divided into two corridors, the effective volume of the secondary settling tank is 500m 3 . The reflux ratio of the nitrifying liquid at the end of the O tank is 4.0, and the reflux ratio of the sludge in the secondary settling tank is 1.0. Original system effluent TN72.9mg·L -1 , NH 3 -N0.2mg·L -1 , TN removal rate is about 83.8%, effluent COD value is 50.0mg·L -1 .
[0028] After testing, it was found that in the above-mentioned A / O process, the ammonia nitrogen dropped to 1.0mg·L at about 75% of the O pool along the water flow direction -1 Below, dissolved oxygen jumps to...
Embodiment 2
[0031] The invention is used to transform and upgrade the high ammonia nitrogen and low C / N wastewater treatment project of a certain nitrogen fertilizer plant.
[0032] The COD of wastewater from a nitrogen fertilizer plant is 600mg·L -1 , TN is 200mg·L -1 , NH 3 -N is 150mg·L -1 , the treated water volume is 10000m 3 d -1 , the existing treatment process is A / O process, and the effective volume of A pool is 5000m 3 , the effective volume of O pool is 10000m 3 , divided into four corridors, the effective volume of the secondary settling tank is 1500m 3 . The reflux ratio of the nitrifying liquid at the end of the O tank is 4.0, and the reflux ratio of the sludge in the secondary settling tank is 0.5. After treatment, the COD of the effluent is 30.0~50.0mg·L -1 , NH 3 -N-1 , but TN still has 36.5mg·L -1 Left and right, it cannot meet the requirements of TN deep processing (ie GB18918-2002, first-class standard).
[0033] The test found that in the above-mentioned A...
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