Enhanced biochemical treatment method for high ammonia-nitrogen wastewater
A technology of biological enhancement and treatment method, which is applied in the field of biological enhancement treatment of high ammonia nitrogen wastewater, can solve the problems such as the limitation of the wide application of biological enhancement technology, the inability to effectively separate the effluent, and the increase of the cost of water treatment, so as to achieve rich biological species and avoid bacteria. Loss, effect of high microbial load
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Embodiment 1
[0029] The method of the present invention is used to treat the landfill leachate, using a combined reactor of a first-stage anaerobic filter + a first-stage anoxic filter + a third-stage biological aerated filter, and employing high-efficiency composite microorganisms Biosystem B350 and B110. COD concentration in raw water is 3800-24000mg / L, NH 3 -N concentration is 1050-2100mg / L, the water temperature of anaerobic filter and anoxic filter is controlled at 30-35°C, the water temperature of biological aerated filter is controlled at 20-28°C, the total residence time is 96h, and the final effluent COD concentration 260-950mg / L, NH 3 -N concentration is 2.0-30.0mg / L. The average COD removal rate reaches over 90%, and the NH 3 The average removal rate of -N reaches over 99%.
Embodiment 2
[0031] The method of the present invention is used to treat the dilution water of pharmaceutical factory production waste water, and the combined reactor of two-stage anoxic filter + three-stage aerated biological filter is adopted, and the high-efficiency composite microorganisms adopted are Biosystem B350 and B500. The influent COD concentration is 950-2500mg / L, the NH3-N concentration is 300-450mg / L, the water temperature of anaerobic filter and anoxic filter is controlled at 30-35℃, and the water temperature of aerated biological filter is controlled at 25-30 ℃, the total residence time is 72h, the final effluent COD concentration is 50-150mg / L, NH 3 -N concentration is 1.0-6.0mg / L.
Embodiment 3
[0033] The coking waste water is treated by the method of the present invention, a combined reactor of a first-stage anaerobic filter + a first-stage anoxic filter + a two-stage aerated biological filter is adopted, and the high-efficiency composite microorganism Biosystem B350 is adopted. Influent COD concentration is 3500-5000mg / L, NH 3 -N concentration is 450-700mg / L, the water temperature of anaerobic filter and anoxic tank is controlled at 30-35°C, the water temperature of biological aerated filter is controlled at 20-30°C, the total residence time is 36-48h, and the final effluent COD The concentration is 80-130mg / L, NH 3-N concentration is 0.2-1.5mg / L.
[0034] It can be seen from the above examples that the method of the present invention has a good treatment effect on different types of high ammonia nitrogen wastewater.
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