Improved powdered activated carbon biological sewage denitrification and dephosphorization treatment device
The technology of a sewage treatment device and powdered activated carbon is applied in the field of improved sewage denitrification and phosphorus removal treatment device, which can solve problems such as cumbersome and achieve the effects of saving usage, efficient removal and reducing sludge amount
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Embodiment 1
[0037] Such as figure 1 As shown, the device of the present invention includes the first anoxic tank, anaerobic tank, the first aerobic tank, the second anoxic tank, the second aerobic tank, the third anoxic tank, the third aerobic tank, and the flocculation tank and clarifiers. The first anoxic tank, the second anoxic tank and the third anoxic tank were added with activated carbon filler, and the dosages were 0.6g / L, 0.3g / L and 0.1g / L respectively. Stirring devices are arranged in the first anoxic pool, the second anoxic pool and the third anoxic pool. An aeration device is arranged in the first aerobic tank, the second aerobic tank and the third aerobic tank. There is no internal circulation between each aerobic pool and anoxic pool. The third aerobic tank includes a sludge return pipe connected to the first anoxic tank. The sewage is divided into three streams and enters the first anoxic pool, the second anoxic pool and the third anoxic pool respectively, and the distri...
Embodiment 2
[0039]The device of the present invention comprises a first anoxic tank, an anaerobic tank, a first aerobic tank, a second anoxic tank, a second aerobic tank, a third anoxic tank, a third aerobic tank, a flocculation tank and a clarification tank . The first anoxic tank and the second anoxic tank are dosed with activated carbon filler, and the dosing amount is 0.8g / L and 0.4g / L respectively. Stirring devices are arranged in the first anoxic pool, the second anoxic pool and the third anoxic pool. An aeration device is arranged in the first aerobic tank, the second aerobic tank and the third aerobic tank. There is no internal circulation between each aerobic pool and anoxic pool. The third aerobic tank also includes a sludge return pipe connected to the first anoxic tank. The sewage is divided into three streams and enters the first anoxic pool, the second anoxic pool and the third anoxic pool respectively, and the distribution coefficient is n1:n2=6:3:1. The volume ratio of...
Embodiment 3
[0041] The device of the present invention comprises a first anoxic tank, an anaerobic tank, a first aerobic tank, a second anoxic tank, a second aerobic tank, a third anoxic tank, a third aerobic tank, a flocculation tank and a clarification tank . Activated carbon filler is added to the first anoxic tank, and the dosage is 1.1 g / L. Stirring devices are arranged in the first anoxic pool, the second anoxic pool and the third anoxic pool. An aeration device is arranged in the first aerobic tank, the second aerobic tank and the third aerobic tank. There is no internal circulation between each aerobic pool and anoxic pool. The third aerobic tank also includes a sludge return pipe connected to the first anoxic tank. The sewage is divided into three streams and enters the first anoxic pool, the second anoxic pool and the third anoxic pool respectively, and the distribution coefficient is n1:n2:n3=7:2:1. The volume ratio of the first aerobic pool to the first anoxic pool is 2:1,...
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