Method for treating ammonia containing wastewater through simultaneous nitrification and denitrification
A simultaneous nitrification and denitrification technology, applied in the field of sewage treatment, can solve the problems of high price, long domestication time, and increased cost, and achieve the effects of saving carbon source and alkalinity, high pollutant removal rate, and low operating cost
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Embodiment 1
[0024] (1) Enrichment culture of aerobic sludge: Take activated sludge from an aerobic aeration tank of a refinery sewage treatment plant, and put it into an aerobic reactor, so that the MLSS in the reactor after inoculating the sludge is 5000mg / L , the method of gradually increasing the concentration of ammonia nitrogen in the matrix is used for enrichment. The initial concentration of ammonia nitrogen in the sewage is 100mg / L, and the concentration of COD is 400mg / L. The concentration of ammonia nitrogen was increased by 100mg / L from the previous time, until the concentration of ammonia nitrogen increased to 1000mg / L, and COD was supplemented while supplementing ammonia nitrogen to maintain the concentration of COD at about 400mg / L. During enrichment: temperature is 25°C; pH 7.5, DO (dissolved oxygen) 2.5mg L -1 about.
[0025] (2) Screening and purification of denitrifying bacteria: Get a certain amount of mud-water mixture obtained in step (1) and dilute different multi...
Embodiment 2
[0029] (1) Enrichment culture of aerobic sludge: Take a certain amount of activated sludge from the aerobic aeration tank of a catalytic sewage treatment plant and put it into the aerobic reactor, so that the MLSS in the reactor after inoculating the sludge is 3000mg / L, the method of gradually increasing the concentration of ammonia nitrogen in the matrix is used for enrichment. The initial concentration of ammonia nitrogen in the sewage is 200mg / L, and the concentration of COD is 600mg / L. Increase by 150mg / L compared with the last time, until it reaches 1500mg / L, supplement COD while supplementing ammonia nitrogen to maintain the COD concentration at about 600mg / L. During enrichment: temperature is 30°C, pH is 7.8, DO (dissolved oxygen) is 3mg·L -1 about.
[0030] (2) Screening and purification of denitrifying bacteria: Get a certain amount of mud-water mixture obtained in step (1) and dilute different multiples and spread it on the beef extract peptone solid medium plate ...
Embodiment 3
[0034] The denitrification sludge obtained in Example 1 is added to the aeration reactor according to the MLSS of 800mg / L to treat the ammoniacal sewage produced in the catalytic cracking catalyst production process. The concentration of main pollutants in this water: COD is 100mg / L on average. L, NH 3 -N is 350 mg / L on average, and the pH is 7.3. First adopt the batch water inlet method, that is, inject the sewage to be treated into the reactor at one time. After running 6 batches, the sludge concentration increases to 1500mg / L, and the removal rate of ammonia nitrogen and total nitrogen reaches more than 90% within 24 hours; On this basis, turn on the water inlet pump and adopt the method of continuous water inlet for treatment. The hydraulic retention time is 24 hours. After 3 days, the system runs stably. The removal rate of ammonia nitrogen reaches 95%, and the removal rate of total nitrogen reaches more than 90%. During the treatment process, methanol was used as a supp...
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