Quick starting method of SBR (Sequencing Batch Reactor) for synchronously denitrifying and removing phosphor
A technology for simultaneous denitrification and phosphorus removal, and rapid start-up. It is applied in chemical instruments and methods, bacteria, water/sludge/sewage treatment, etc., to improve the effluent effect and shorten the start-up time.
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Embodiment 1
[0026] The SBR system was operated under anaerobic / aerobic conditions, with instantaneous water inflow for 5 minutes, anaerobic stirring for 2.5 hours, aerobic continuous aeration for 3 hours, sedimentation for 1 hour, and drainage for 1.5 hours. In the aerobic stage, the DO concentration in the water was kept at 2-4mg / L, and in the anaerobic stage, the DO concentration in the water was less than 0.2mg / L. The water temperature was controlled at 20-25°C, and the pH value was adjusted to 7-8. Run 20d. The removal rate of ammonia nitrogen reaches 90%, and the removal rate of TP reaches 70%;
[0027] Change the operation mode of the system to: instantaneous water inflow for 5 minutes, anaerobic stirring for 2.5 hours, aerobic continuous aeration for 1.5 hours, anoxic stirring for 1.5 hours, aerobic aeration for 0.5 hours, sedimentation for 1 hour, and drainage for 1 hour. In the aerobic and anaerobic phases, the DO concentration and water temperature remain unchanged, and the slu...
Embodiment 2
[0032] The SBR system was operated under anaerobic / aerobic conditions, with instantaneous water inflow for 5 minutes, anaerobic stirring for 2.5 hours, aerobic continuous aeration for 3 hours, sedimentation for 1 hour, and drainage for 1.5 hours. In the aerobic stage, the DO concentration in the water was kept at 2-4mg / L, and in the anaerobic stage, the DO concentration in the water was less than 0.2mg / L. The water temperature was controlled at 20-25°C, and the pH value was adjusted to 7-8. Run 30d. The removal rate of ammonia nitrogen reaches 99%, and the removal rate of TP reaches 80%. Change the operation mode of the system to: instantaneous water inflow for 5 minutes, anaerobic stirring for 2.5 hours, aerobic continuous aeration for 1.5 hours, anoxic stirring for 1.5 hours, aerobic aeration for 0.5 hours, sedimentation for 1 hour, and drainage for 1 hour. In the aerobic and anaerobic phases, the DO concentration and water temperature remain unchanged, and the sludge is di...
Embodiment 3
[0036] The SBR system was operated under anaerobic / aerobic conditions, with instantaneous water inflow for 5 minutes, anaerobic stirring for 2.5 hours, aerobic continuous aeration for 3 hours, sedimentation for 1 hour, and drainage for 1.5 hours. In the aerobic stage, the DO concentration in the water was kept at 2-4mg / L, and in the anaerobic stage, the DO concentration in the water was less than 0.2mg / L. The water temperature was controlled at 20-25°C, and the pH value was adjusted to 7-8. Run 25d. The removal rate of ammonia nitrogen reaches 95%, and the removal rate of TP reaches 78%.
[0037] Change the operation mode of the system to: instantaneous water inflow for 5 minutes, anaerobic stirring for 2.5 hours, aerobic continuous aeration for 1.5 hours, anoxic stirring for 1.5 hours, aerobic aeration for 0.5 hours, sedimentation for 1 hour, and drainage for 1 hour. In the aerobic and anaerobic phases, the DO concentration and water temperature remain unchanged, and the slu...
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