Biologically enhanced treatment method for medium-and-low concentration ammonia-nitrogen wastewater
A low-concentration ammonia-nitrogen, bioaugmentation technology, applied in the field of biological treatment of low-concentration ammonia-nitrogen wastewater, can solve the problems of difficult enrichment and easy loss of ammonia oxidizing bacteria, and achieve increased solid residence time, fast mass transfer, Effect of Reducing Reactor Volume
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Embodiment 1
[0026] Adopt method of the present invention to process ammonia nitrogen simulated waste water, water quality is as follows: ammonia nitrogen 300mg / L, COD cr 500mg / L, put the immobilized microbial carrier into a 1L aerated biological fluidized bed according to the dosage of 15% (W / W), the pH of the influent water is about 8, the water temperature is about 30°C, and the dissolved oxygen is 5mg / L About, when the residence time is 2h, 4h, 6h, 8h, the concentration of ammonia nitrogen in the effluent is 121.01mg / L, 71.65mg / L, 22.81mg / L, 12.65mg / L; the concentration of nitrite nitrogen in the effluent is 82.11 mg / L, 117.40mg / L, 167.13mg / L, 193.72mg / L; the nitrate nitrogen in the effluent was all within 20mg / L. Under the condition of 8h residence time, the removal rate of ammonia nitrogen was 95.7%, and the reactor effluent NO 2 - / NO x - maintained above 90%. NO x The concentration can be reduced to less than 10mg / L.
Embodiment 2
[0028] Adopt method of the present invention to process ammonia nitrogen simulated waste water, water quality is as follows: ammonia nitrogen 300mg / L, COD cr 500mg / L, put the immobilized microbial carrier into a 1L aerated biological fluidized bed according to the dosage of 5% (W / W), the pH of the influent water is about 8, the water temperature is about 30°C, and the dissolved oxygen is 5mg / L About, when the residence time is 2h, 4h, 6h, 8h, 10h, the concentration of ammonia nitrogen in the effluent is 177.37mg / L, 120.22mg / L, 104.03mg / L, 68.68mg / L, 34.24mg / L; The concentrations of nitrate nitrogen were 30.91mg / L, 41.78mg / L, 63.02mg / L, 100.06mg / L, and 132.69mg / L respectively; the nitrate nitrogen in the effluent was all within 20mg / L. Under the condition of 10h residence time, the removal rate of ammonia nitrogen is 88.6%, and the reactor effluent NO 2 - / NO x - maintained above 90%. NO x The concentration can be reduced to less than 10mg / L.
Embodiment 3
[0030] Adopt the inventive method to process synthetic ammonia industrial waste water, water quality is as follows: ammonia nitrogen 120-300mg / L, COD cr200-400mg / L, continuous treatment of wastewater according to the scale of 100mL / h, the process flow of the device is anoxic tank-aerated biological fluidized bed, in which, the residence time of anoxic tank is 11h, and the residence time of aerated biological fluidized bed 11h, the dosage of immobilized carrier in the aerated biological fluidized bed embedding method is 15%, and the ammonia nitrogen in the effluent is under the conditions of influent pH=7-8, water temperature 25-35℃, dissolved oxygen 3-5mg / L The concentration is 5-15mg / L, and the removal rate of ammonia nitrogen is over 90%.
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