A cc-hbdp treatment process for livestock and poultry breeding wastewater
A technology for livestock and poultry breeding wastewater and treatment process, which is applied in animal husbandry wastewater treatment, multi-stage water treatment, water/sewage treatment, etc. It can solve the problem of influent COD not being too high, achieve less sludge production, and reduce organic load , the effect of low energy consumption
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Embodiment 1
[0027] Example 1: In step (1), the coagulant in the coagulation tank is polyaluminum chloride, the dosage is 50 mg / L, the stirring speed is 50 r / min, and the residence time is 5 min; by controlling the dosage of the coagulant , so that the C / N ratio of the sewage entering the mixed denitrification tank is 1:1.
[0028] In this embodiment, in step (2), the hydraulic retention time in the clarifier is 1h, and the aperture of the first solid-liquid separation device is 25 μm; the captured carbon source is discharged through the vent valve 8 below the clarifier 5 for collection.
[0029] In this embodiment, in step (3), the dissolved oxygen in the mixed denitrification tank is controlled at 0.2 mg / L and the pH is controlled at 7.8 by controlling the aeration amount of the aeration device 10; the braided belt is vertically suspended in the mixed denitrification tank The density of the braided packing 11 is 50 pieces per square meter.
Embodiment 2
[0030] Example 2: In step (1), the coagulant in the coagulation tank is polyaluminum chloride, the dosage is 400 mg / L, the stirring speed is 300 r / min, and the residence time is 20 min; by controlling the dosage of the coagulant , so that the C / N ratio of the sewage entering the mixed denitrification tank is 3:1.
[0031] In this embodiment, in step (2), the hydraulic retention time in the clarifier is 3 h, and the aperture of the first solid-liquid separation device is 150 μm; the captured carbon source is discharged through the vent valve 8 below the clarifier 5 for collection.
[0032] In this embodiment, in step (3), the dissolved oxygen in the mixed denitrification tank is controlled at 0.5 mg / L and the pH is controlled at 8.2 by controlling the aeration amount of the aeration device 10; the braided belt is vertically suspended in the mixed denitrification tank The density of the braided packing 11 is 100 pieces per square meter.
Embodiment 3
[0033] Example 3: In step (1), the coagulant in the coagulation tank is polyaluminum chloride, the dosage is 200 mg / L, the stirring speed is 300 r / min, and the residence time is 5 min; The C / N ratio of the sewage entering the mixed denitrification tank is 2:1.
[0034] In this example, in step (2), the hydraulic retention time in the clarifier is 3 h, and the aperture of the first solid-liquid separation device is 70 μm; the captured carbon source is discharged through the vent valve 8 below the clarifier 5 for collection.
[0035]In this embodiment, in step (3), the dissolved oxygen in the mixed denitrification tank is controlled at 0.2 mg / L and the pH is controlled at 8.0 by controlling the aeration amount of the aeration device 10; the braided belt is vertically suspended in the mixed denitrification tank The density of the braided packing 11 is 70 pieces per square meter.
[0036] The influent COD concentration of livestock and poultry breeding wastewater in a rural area ...
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