Integrated device and method for enhancing denitrification and dephosphorization of dispersed village and town sewage
A decentralized technology for nitrogen and phosphorus removal, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problems of low efficiency, inconvenient operation and maintenance, nitrogen and phosphorus removal Ineffective and other problems, to achieve the effect of increasing impact load, balancing reaction efficiency and economic cost
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Embodiment approach 1
[0032] Use village and town sewage with high phosphorus concentration as the treatment object (pH=6-8, COD=300-400mg / L, NH 4 + -N=35-45 mg / L, TN=40-50 mg / L, TP=3-5 mg / L). The positions of the non-porous partition 25 and the porous partition 26 coincide with the anaerobic filter zone H and the contact oxidation zone I respectively along the water inlet direction, the composite zone C is transformed into the contact oxidation zone I, and the main body of the device 1 is along the water inlet direction In turn, it is anaerobic filter A, B area, contact oxidation I, D, E, F area and effluent area G. According to the filler filtration rate, adjust the influent flow rate, control the hydraulic retention time of the contact oxidation zone I and the water outlet zone G to be 30min and 40min respectively, the anaerobic filter A and B zones are each 80min, and the contact oxidation D, E, and F are each 80min. 60min, the total hydraulic retention time of the reaction is about 6.83h. C...
Embodiment approach 2
[0034] Use village and town sewage containing organic matter and high phosphorus concentration as the treatment object (pH=6-8, COD=500-600mg / L, NH 4 + -N=35-45 mg / L, TN=40-50 mg / L, TP=3-5 mg / L). The positions of the non-porous partition 25 and the porous partition 26 coincide with the contact oxidation zone I and the anaerobic filter zone H respectively along the water inlet direction, the compound zone C is transformed into the anaerobic filter zone H, and the main body of the device 1 along the inlet The water direction is the anaerobic filter A, B, H area, the contact oxidation area D, E, F and the water outlet area G. According to the filtration rate of the packing, the inflow flow is adjusted to control the flow rate of the anaerobic filter H area and the water outlet area G. The hydraulic retention time is 40min, the anaerobic filter A, B area is 80min each, the contact oxidation D, E, F area is 60min, and the total hydraulic retention time of the reaction is 7.0h. Co...
Embodiment approach 3
[0036] Use village and town sewage with high concentration of ammonia nitrogen and phosphorus as the treatment object (pH=6-8, COD=300-400mg / L, NH 4 + -N=50-55 mg / L, TN=55-60 mg / L, TP=3-5 mg / L). The positions of the non-porous partition 25 and the porous partition 26 coincide with the anaerobic filter zone H and the contact oxidation zone I respectively along the water inlet direction, the composite zone C is transformed into the contact oxidation zone I, and the main body of the device 1 is along the water inlet direction In turn, it is anaerobic filter A, B area, contact oxidation I, D, E, F area and effluent area G. According to the packing filtration rate, adjust the influent flow rate, control the hydraulic retention time of the contact oxidation zone I and the water outlet zone G to be 30min and 40min respectively, the anaerobic filter A and B zones are each 80min, and the contact oxidation zones D, E and F are each is 60min, and the total hydraulic retention time of t...
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