A sewage treatment device with a parallel structure
A sewage treatment device, parallel technology, applied in the direction of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., can solve the problem that the waste water cannot be fully reached, and achieve simple and efficient sewage treatment equipment, The effect of reducing the amount of sludge and saving the amount of use
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Embodiment 1
[0068] Such as figure 1 As shown, the device of the present invention includes a first anoxic tank and a second anoxic tank, a first aerobic tank, a third anoxic tank, a second aerobic tank, a flocculation tank and a clarification tank connected in parallel. The first anoxic pool and the third anoxic pool are dosed with activated carbon filler, and the dosing amount is 1.5g / L and 0.5g / 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 and the second aerobic tank. There is no internal circulation between each aerobic pool and anoxic pool. 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 n(1):n(2):n(3)=7:2:0.2:0.8. The volume ratio of the first aerobic pool to the first anoxic pool is 2:1, the volume ratio of the first aerobic ...
Embodiment 2
[0070] Such as figure 2 As shown, the device of the present invention includes a first anoxic tank, a first aerobic tank and a second aerobic tank connected in parallel, a second anoxic tank, a third 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 0.7g / L and 0.3g / 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, the second aerobic tank and the third 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 pool to the first anoxic pool is 1:1, the volume ratio of the second aerobic pool to the first anoxic pool is 1:1, an...
Embodiment 3-4
[0072] In front of the above-mentioned embodiment 1-2, a pretreatment device is added, that is, a series electrocatalytic oxidation and photocatalytic oxidation device, and the anode in the electrolytic system of the electrocatalytic oxidation is Ti / PbO 2 The anode and cathode are Ti cathodes, and the current density is 20mA cm -2 ; The photocatalytic oxidation is based on TiO 2 as catalyst, H 2 o 2 As an oxidizing agent, it is carried out under ultraviolet light irradiation, where TiO 2 The dosage can be reduced to 10% of the existing known dosage.
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