Method and device for regulating and controlling sludge load to cope with instantaneous organic matter impact and application
A technology of sludge load and organic matter, applied in the direction of water pollutants, chemical instruments and methods, water/sludge/sewage treatment, etc., can solve problems such as rising and biochemical pools cannot run stably, and achieve obvious reduction and pollutants Removes effects that are stable and highly usable
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Embodiment 1
[0077] This embodiment is a simulation run of the laboratory 2 The O reactor is used for transient organic matter shock research. The operating environment of the reactor includes: water temperature 20-22 ° C, the volume ratio of the anaerobic, anoxic and aerobic sections of the reactor is 1:1:2, the raw water enters from the anaerobic section, and the hydraulic The residence time is 20h, the average sludge concentration is 3500mg / L, the reflux ratio in the nitrifying liquid is 200%, and the sludge reflux ratio is 100%. The instantaneous organic matter impact concentration is about 800 mg / L, and the instantaneous impact time is 2 hours. After the impact, the COD of the effluent rises sharply, and the intermittent return operation of the sludge tank is regulated. The specific measures are as follows:
[0078] The sludge in the sludge thickening tank 14 is backflowed, the first valve 4 is opened, and the sludge lifting pump 1 is started to drive the sludge in the sludge thickeni...
Embodiment 2
[0081] This embodiment is a simulation run of the laboratory 2 The O reactor is used for transient organic matter shock research. The operating environment of the reactor includes: water temperature 20-22 ° C, the volume ratio of the anaerobic, anoxic and aerobic sections of the reactor is 1:1:2, the raw water enters from the anaerobic section, and the hydraulic The residence time is 20h, the average sludge concentration is 3500mg / L, the reflux ratio in the nitrifying liquid is 200%, and the sludge reflux ratio is 100%. The instantaneous organic matter impact concentration is about 1200 mg / L, and the instantaneous impact time is 2 hours. After the impact, the COD of the effluent rises sharply. The intermittent return operation of the sludge tank is regulated. The specific measures are as follows:
[0082] The sludge in the sludge thickening tank 14 is backflowed, the first valve 4 is opened, and the sludge lifting pump 1 is started to drive the sludge in the sludge thickening ...
Embodiment 3
[0085] This embodiment is a simulation run of the laboratory 2 The O reactor is used for transient organic matter shock research. The operating environment of the reactor includes: water temperature 20-22 ° C, the volume ratio of the anaerobic, anoxic and aerobic sections of the reactor is 1:1:2, the raw water enters from the anaerobic section, and the hydraulic The residence time is 20h, the average sludge concentration is 3500mg / L, the reflux ratio in the nitrifying liquid is 200%, and the sludge reflux ratio is 100%. The instantaneous organic matter impact concentration is about 1600 mg / L, and the instantaneous impact time is 2 hours. After the impact, the COD of the effluent rises sharply, and the intermittent return operation of the sludge tank is regulated. The specific measures are as follows: the sludge in the sludge concentration tank 14 returns the sludge, and the first valve is opened. 4. Start the sludge lifting pump 1 to pump the sludge in the sludge thickening ta...
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