Bioaugmentation treatment technology of high ammonia nitrogen wastewater
A bio-enhancement and treatment process technology, applied in the field of water treatment, can solve the problems that affect the stable operation of the system and the effluent quality, increase the capital construction investment and operating costs, and the total hydraulic retention time of the system, etc. , the effect of increasing the volume load
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Embodiment 1
[0027] Example 1, using the present invention to treat wastewater from a saccharin factory, using a combined process of primary anoxic pool + tertiary aerobic filter + membrane pool, the enzyme floating filler used is enzyme floating A series of ionic enzymatic suspension fillers. Influent COD Cr The concentration is 2000-13000mg / L, NH 3 -N concentration is 1000-5500mg / L, anoxic tank temperature is 28-32℃, aerobic filter temperature is 25-30℃, total hydraulic retention time is 120h, no need to add carbon source, but only need to add about 180mg / L alkali degree (as CaCO 3 count), effluent COD Cr The concentration is 20-300mg / L, NH 3 -N concentration is 0.65-30mg / L. COD Cr The average removal rate is above 90%, NH 3 The average removal rate of -N is above 99%.
Embodiment 2
[0028] Example 2, using the present invention to treat wastewater from chemical fertilizer plants, using a combined process of one-stage anoxic pool + two-stage aerobic filter + membrane pool, and the enzyme floating filler used is enzyme floating A series of ionic enzymatic suspension fillers. Influent COD Cr The concentration is 300-700mg / L, NH 3 -N concentration is 200-400mg / L, anoxic pool temperature is 30-35℃, aerobic filter temperature is 20-30℃, total hydraulic retention time is 72h, only need to add about 200mg / L methanol as carbon source, effluent COD Cr The concentration is 10-50mg / L, NH 3 -N concentration is 0.10-2.0mg / L. COD Cr The average removal rate is above 90%, NH 3 The average removal rate of -N is above 99%.
Embodiment 3
[0029] Example 3, using the present invention to treat wastewater from a coking plant, using a combined process of primary anoxic pool + tertiary aerobic filter + membrane pool, the enzyme floating filler used is enzyme floating A series of ionic enzymatic suspension fillers. Influent COD Cr The concentration is 2500-5500mg / L, NH 3-N concentration is 300-600mg / L, anoxic tank temperature is 30-35°C, aerobic filter temperature is 25-30°C, total hydraulic retention time is 64h, effluent COD Cr The concentration is 40-150mg / L, NH 3 -N concentration is 0.20-4.0mg / L. COD Cr The average removal rate is above 90%, NH 3 The average removal rate of -N is above 99%.
[0030] It can be seen from the above examples that the present invention has good removal effects on different types of high ammonia nitrogen wastewater.
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