A coupled wastewater treatment device and a treatment method for petrochemical secondary effluent
A wastewater treatment and secondary effluent technology, which is applied in special compound water treatment, natural water treatment, water/sewage treatment, etc., can solve the problems of poor treatment effect and low phosphorus removal effect of biological aerated filter, and achieve reduction The effect of operating cost, reducing dosage and improving removal rate
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Embodiment 1
[0029] Such as figure 1 As shown, a coupled wastewater treatment device includes a biological aerated filter 7 and an ozone catalytic oxidation tower 14, the biological aerated filter 7 is a downward flow type, and the first water intake area is sequentially from top to bottom 21. The first filling area 22, the first water outlet area 23, the first aeration pan 24 is arranged at the lower part of the first water outlet area 23, and the first aeration pan 24 is arranged at the lower part of the biological aerated filter 7. The first water outlet 25 that a water outlet area 23 links to each other; Described ozone catalytic oxidation tower 14 is a sealed tower, is successively from top to bottom the second water inlet area 26, the second packing area 27 and the second water outlet area 28, in the The bottom of the second water outlet area 28 is provided with a second aeration pan 29, and the top of the ozone catalytic oxidation tower 14 is provided with a second water inlet 30 co...
Embodiment 2
[0038] The COD of the secondary effluent of a comprehensive sewage treatment plant in a large petrochemical industrial park is between 70-90mg / L, with an average of 74.5mg / L. 4 The dosage is 9mg / L, the biological aerated filter is filled with ceramsite, the filling rate is 70%, the air-water ratio is 3:1, the empty tower hydraulic retention time is 3h, the ozone dosage is 10mg / L, and the contact oxidation Time 1h. At the same time, a comparative test was carried out, and FeSO was not added to the wastewater entering the biological aerated filter. 4 , and the other parameters are the same. Such as figure 2 As shown, the results show that due to the addition of FeSO at the front end of the biological aerated filter 4 Due to the coupling catalysis formed, the average COD of the final effluent is 39.9 mg / L, while the average COD of the effluent without using the comparison device of the present invention is 50.6 mg / L. It can be seen that using the device and operating paramet...
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