High-efficiency biological treatment method of high-organic matter high-kjeldahl type nitrogen chemical industry wastewater
A technology for chemical wastewater and biological treatment, applied in chemical instruments and methods, water/sludge/sewage treatment, aerobic and anaerobic process treatment, etc. Nitrogen, etc.
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Embodiment 1
[0013] 1) Inject 500L of chemical wastewater raw water into the distribution tank, add sodium bicarbonate to make the ratio of Kjeldahl nitrogen / alkalinity to 7.14, add sodium dihydrogen phosphate with a concentration of 50mg / L, stir for 5 minutes, and settle for 0.5 hours;
[0014] 2) The chemical wastewater treated by water distribution in the water distribution tank is continuously fed into the first-stage anaerobic tank through the water inlet pump at a flow rate of 10L / h, and stirred at a stirring speed of 80r / h and a temperature of 20°C; the effluent enters the first-stage aerobic tank The aerobic pool has an air-to-water ratio of 50 / 1 and a temperature of 25°C; the organic matter in the wastewater is removed through the hydrolytic acidification of the anaerobic pool and the aerobic oxidation of the aerobic pool, and the organic nitrogen is released to be converted into ammonia nitrogen; the effluent enters the middle Sedimentation tank, settling for 4 hours, the activate...
Embodiment 2
[0018] 1) Inject 500L of chemical wastewater raw water into the distribution tank, add sodium bicarbonate to make the ratio of Kjeldahl nitrogen / alkalinity to 7.14, add sodium dihydrogen phosphate with a concentration of 50mg / L, stir for 10 minutes, and settle for 1 hour;
[0019] 2) The chemical wastewater treated by water distribution in the water distribution tank is continuously fed into the first-stage anaerobic tank through the water inlet pump at a flow rate of 15L / h, and stirred at a stirring speed of 120r / h and a temperature of 25°C; the effluent enters the first-stage aerobic tank The gas-water ratio of the aerobic pool is 60 / 1, and the temperature is 28°C; the organic matter in the wastewater is removed through the hydrolytic acidification of the anaerobic pool and the aerobic oxidation of the aerobic pool, and the organic nitrogen is released and converted into ammonia nitrogen; the effluent enters the middle Sedimentation tank, settling for 8 hours, the activated s...
Embodiment 3
[0023] The schematic diagram of the technological process of this embodiment is shown in the accompanying drawings. The effective volume and hydraulic retention time (flow rate: 10L / h) of each unit are as follows:
[0024] surface
[0025]
[0026] 1) Inject 500L of chemical wastewater raw water into the distribution tank, add sodium bicarbonate to make the ratio of Kjeldahl nitrogen / alkalinity to 7.14, add sodium dihydrogen phosphate with a concentration of 50mg / L, stir for 10 minutes, and settle for 0.5 hours;
[0027] 2) The chemical wastewater treated by water distribution in the water distribution tank is continuously fed into the first-stage anaerobic tank through the water inlet pump at a flow rate of 10L / h, and stirred at a stirring speed of 120r / h and a temperature of 20°C; the effluent enters the first-stage aerobic tank The aerobic pool has an air-to-water ratio of 50 / 1 and a temperature of 25°C; the organic matter in the wastewater is removed through the hydrol...
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