Method for processing nitrobenzene and aniline waste water
A technology for aniline wastewater and nitrobenzene, applied in chemical instruments and methods, multi-stage water/sewage treatment, water/sludge/sewage treatment, etc., can solve problems such as poor safety, high treatment cost, and difficult sludge disposal , achieve strong impact load resistance, remove ammonia nitrogen and total nitrogen, and avoid secondary pollution
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Embodiment 1
[0028] The present invention is used to treat nitrobenzene and aniline waste water from a company’s organic chemical plant. The raw water COD concentration is 2000mg / L, nitrobenzene concentration is 100mg / L, aniline concentration is 500mg / L, petroleum is 100mg / L, and the treatment capacity is 1200m 3 / d, the water temperature in the I-AF reactor and I-BAF reactor is controlled at 20°C-40°C, the hydraulic retention time is 13h and 16h respectively, the final effluent COD concentration is 100mg / L, and the nitrobenzene concentration is 2mg / L , the concentration of aniline is 1mg / L and that of petroleum is 8mg / L.
Embodiment 2
[0030] Using the present invention to treat nitrobenzene and aniline wastewater from a polyurethane joint-stock company, the raw water COD concentration is 2000-3500mg / L, the nitrobenzene concentration is 150-300mg / L, the aniline concentration is 400-800mg / L, and the treatment capacity is 480m 3 / d, the water temperature in the I-AF reactor and I-BAF reactor is controlled at 20°C-40°C, the hydraulic retention time is 20h and 26h respectively, the final effluent COD concentration is 30-150mg / L, and the nitrobenzene concentration is 0.5 -2mg / L, the concentration of aniline is 0.2-1mg / L.
Embodiment 3
[0032] Using the present invention to treat nitrobenzene and aniline wastewater of a certain company, the COD concentration of the raw water is 2000-4200mg / L, the nitrobenzene concentration is 100-300mg / L, the aniline concentration is 600-1000mg / L, and the chlorobenzene concentration is 50-100mg / l, the concentration of formaldehyde is 100-200mg / l, the concentration of chloride ion is 10000-30000mg / l, and the processing capacity is 1000m 3 / d, the water temperature in the I-AF reactor and I-BAF reactor is controlled at 20°C-40°C, the hydraulic retention time is 26h and 30h respectively, the final effluent COD concentration is 30-100mg / L, and the nitrobenzene concentration is 1mg / L, the concentration of aniline is 0.3-0.7mg / L.
[0033] It can be seen from the above examples that the present invention has good treatment effects on nitrobenzene and aniline wastewaters of different water qualities.
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