A sewage treatment device for multi-stage non-reflux powdered activated carbon bioactive treatment
The technology of a sewage treatment device and powder activated carbon is applied in the field of improved powder activated carbon sewage treatment device, which can solve the problems of cumbersome process and large amount of sludge, and achieve the effects of efficient removal, reduction of sludge amount and saving of usage amount.
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Embodiment 1
[0039] Such as figure 1 As shown, the device of the present invention includes a first anoxic tank, a first aerobic tank, a second anoxic tank, a second aerobic tank, a flocculation tank and a clarification tank. The first anoxic tank and the second anoxic tank were dosed with activated carbon filler, and the dosages were 1.8g / L and 0.2g / L respectively. Stirring devices are arranged in the first anoxic tank and the second anoxic tank. An aeration device is arranged in the first aerobic tank and the second aerobic tank. There is no internal circulation between each aerobic pool and anoxic pool. The sewage is divided into two streams and enters the first anoxic pool and the second anoxic pool respectively, and the distribution coefficient is n1:n2=6:4. The volume ratio of the first aerobic tank to the first anoxic tank is 2:1, and the volume ratio of the second aerobic tank to the second anoxic tank is 1:1. The remaining bio-carbon sludge in the clarifier is discarded.
Embodiment 2
[0041] Such as figure 2 As shown, the device of the present invention includes a first anoxic tank, a first aerobic tank, a second anoxic tank, a second aerobic tank, a flocculation tank and a clarification tank. The first anoxic tank and the second anoxic tank were dosed with activated carbon filler, and the dosages were 0.6g / L and 0.4g / L respectively. Stirring devices are arranged in the first anoxic tank and the second anoxic tank. An aeration device is arranged in the first aerobic tank and the second aerobic tank. There is no internal circulation between each aerobic pool and anoxic pool. The sewage is divided into two streams and enters the first anoxic pool and the second anoxic pool respectively, and the distribution coefficient is n1:n2=5:5. The volume ratio of the first aerobic tank to the first anoxic tank is 2:1, and the volume ratio of the second aerobic tank to the second anoxic tank is 1.5:1. The remaining bio-carbon sludge in the clarifier is discarded.
Embodiment 3
[0043] Such as image 3 As shown, the device of the present invention includes a first anoxic tank, a first aerobic tank, a second anoxic tank, a second aerobic tank, a flocculation tank and a clarification tank. Activated carbon filler is added in the first anoxic tank, and the dosage is 1.5g / L. Stirring devices are arranged in the first anoxic tank and the second anoxic tank. An aeration device is arranged in the first aerobic tank and the second aerobic tank. There is no internal circulation between each aerobic pool and anoxic pool. The sewage is divided into two streams and enters the first anoxic pool and the second anoxic pool respectively, and the distribution coefficient is n1:n2=8:2. The volume ratio of the first aerobic tank to the first anoxic tank is 2:1, and the volume ratio of the second aerobic tank to the second anoxic tank is 1:1. The remaining bio-carbon sludge in the clarifier is discarded.
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