Advanced treatment device and method for aniline wastewater
A technology for advanced treatment of waste water, applied in multi-stage water treatment, water/sewage treatment, biological water/sewage treatment, etc., to achieve good purification effect, low treatment cost, and reduced treatment cost
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Embodiment 1
[0023] Wastewater containing 2,3-dichlorobenzidine from a dye intermediate production enterprise: water volume 50m 3 / h, COD is 4500mg / L, and salt content is 12%. The treatment device and method provided by the present invention are used for treatment: the hydraulic retention time of the wastewater in the membrane extraction reactor 3 is 12 hours, the extracted water enters the ozone catalytic oxidation reactor 7 and is oxidized for 60 minutes, and the concentration of ozone dosing is 200 mg / L, the circulating volume of the extract is 150m 3 / h, the hydraulic retention time of the extract in the membrane extraction reactor 3 is 4 hours, and the hydraulic retention time in the biochemical reactor 14 is 30 hours. Outlet 9 water volume 50m 3 / h, COD is 50mg / L, salt content is 12%, and the treatment cost is 5.5 yuan / m 3 .
Embodiment 2
[0025] Aniline-containing wastewater from a pesticide production enterprise: water volume 100m 3 / h, COD is 1200mg / L, and salt content is 8%. The treatment device and method provided by the present invention are used for treatment: the hydraulic retention time of the wastewater in the membrane extraction reactor 3 is 4 hours, the extracted water enters the ozone catalytic oxidation reactor 7 and is oxidized for 15 minutes, and the concentration of ozone dosing is 50 mg / L, the circulating volume of the extract is 200m 3 / h, the hydraulic retention time of the extract in the membrane extraction reactor 3 is 2 hours, and the hydraulic retention time of the extract in the biochemical reactor 14 is 10 hours. Outlet 9 water volume 100m 3 / h, COD is 42mg / L, salt content is 8%, and the treatment cost is 3.6 yuan / m 3 .
Embodiment 3
[0027] Wastewater containing aniline and chloramine in a pharmaceutical production enterprise: water volume 200m 3 / h, COD is 3500mg / L, and salt content is 10%. The treatment device and method provided by the present invention are used for treatment: the hydraulic retention time of the wastewater in the membrane extraction reactor 3 is 8 hours, the extracted water enters the ozone catalytic oxidation reactor 7 and is oxidized for 30 minutes, and the concentration of ozone dosing is 100 mg / L, the circulation volume of extract liquid is 400m 3 / h, the hydraulic retention time of the extract in the membrane extraction reactor 3 is 3 hours, and the hydraulic retention time of the extract in the biochemical reactor 14 is 20 hours. Outlet 9 water volume 200m 3 / h, COD is 45mg / L, salt content is 10%, and the treatment cost is 4.0 yuan / m 3 .
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