Device and method for removing pollutants in rural domestic sewage
A technology for domestic sewage and pollutants, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., to achieve low investment, improve treatment efficiency, and occupy a small area
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Embodiment 1
[0038]The above-mentioned device for removing pollutants in rural domestic sewage is used to treat domestic sewage generated in a village. The production volume of domestic sewage is 50 tons per day, and the treatment is required to meet the "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002) It is discharged into the surrounding water body after meeting the first-level A standard.
[0039] The domestic sewage first enters the three-compartment septic tank 1, and the domestic sewage is treated by the three-stage septic tank 1, and then passes through the filter screen 2 to intercept large suspended particle pollutants, and then enters the anaerobic suspended packing bed reaction tank 3 for pretreatment;
[0040] The anaerobic suspended packing bed reaction tank 3 adopts an upflow structure, the suspended packing adopts porous spherical packing, and the hydraulic retention time of the anaerobic suspended packing bed is controlled at 5h;
[0041] Th...
Embodiment 2
[0046] The production of domestic sewage in a certain village is 150 tons per day. The domestic sewage first enters the three-compartment septic tank 1, and after being treated in the three-compartment septic tank 1, the domestic sewage passes through the filter screen 2 to intercept large suspended particle pollutants, and then enters the exhaust Oxygen suspended packed bed reaction tank 3 is pretreated;
[0047] The anaerobic suspended packing bed reaction tank 3 adopts an upflow structure, the suspended packing adopts porous spherical packing, and the hydraulic retention time of the anaerobic suspended packing bed is controlled to 5.5h;
[0048] The effluent from the anaerobic suspended packed bed reaction tank 3 enters the hypoxic aeration tank 4 for biochemical reaction to further remove organic matter in the sewage. The hydraulic retention time of oxygen aeration tank 4 is 2.5h;
[0049] The effluent from the hypoxic aeration tank 4 enters the vertical flow sedimentatio...
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