Method for treating wastewater generated in production of hexabromocyclododecane
A technology for hexabromocyclododecane and production wastewater, which is applied in the fields of natural water body treatment, water/sewage multi-stage treatment, reduced water/sewage treatment, etc. Oxidants or catalysts are expensive, and the treatment effect cannot meet the discharge requirements, so as to improve the effect of wastewater treatment, increase the daily treatment capacity, and improve the flocculation effect.
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Embodiment 1
[0040] Discharge the HBCD production wastewater containing chloroform, isobutanol and a small amount of products into the regulating tank. The pH value of the wastewater is 8.5, the COD value is 12000mg / L, the bromide ion content is 6000mg / L, and the ammonia nitrogen content It is 1000mg / L. First adjust the pH value to 3 with waste sulfuric acid, transfer it to the reduction reaction tank, add a mixture of iron powder and aluminum powder with a relative waste water volume of 1Kg / t, and add sodium carbonate and magnesium sulfate with a relative waste water volume of 0.5Kg / t The mixture was reduced under stirring for 3 hours, and then the waste water after the reaction was transferred to the flocculation sedimentation tank, and sodium slag was added to adjust the pH value of the waste water to be neutral, and polyacrylamide with a relative waste water volume of 0.02Kg / t was added to make the catalytic reduction reaction The produced iron and aluminum ions form hydroxides and cau...
Embodiment 2
[0042] Discharge the HBCD production wastewater containing chloroform, isobutanol and a small amount of products into the adjustment tank. The pH of the wastewater is 9.0, the COD value is 12500mg / L, the bromide ion content is about 6350mg / L, and the ammonia nitrogen content It is 1500mg / L. First adjust the pH value to 3.5, transfer to the reduction reaction tank, add a mixture of iron powder and aluminum powder with a relative waste water volume of 2Kg / t, add a mixture of sodium sulfate and magnesium chloride with a relative waste water volume of 0.3Kg / t, and stir The reduction reaction was carried out for 3 hours, and then the waste water after the reaction was transferred to the flocculation sedimentation tank, and the pH value of the waste water was adjusted to be neutral, so that the iron and aluminum ions produced by the catalytic reduction reaction formed hydroxides, resulting in flocculation, and the supernatant after flocculation and precipitation The liquid is discha...
Embodiment 3
[0044]Discharge the HBCD production wastewater containing chloroform, isobutanol and a small amount of products into the adjustment tank. The pH of the wastewater is 9.5, the COD value is 11300mg / L, the bromide ion content is about 5900mg / L, and the ammonia nitrogen content It is 1100mg / L. First use waste sulfuric acid to adjust the pH value to 4, transfer it to the reduction reaction tank, add iron powder with a relative waste water volume of 5Kg / t, add sodium carbonate with a relative waste water volume of 0.1Kg / t, and reduce the reaction for 3-4 hours under stirring. hours, and then the waste water after the reaction is transferred to the flocculation sedimentation tank, and the pH value of the waste water is adjusted to be neutral, so that the iron and aluminum ions generated by the catalytic reduction reaction form hydroxides to produce flocculation, and the supernatant after flocculation and precipitation is discharged into the subsequent In the biochemical treatment sec...
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