Method for effectively removing organic matters in wastewater from nitrochlorobenzene production
A technology for the production of nitrochlorobenzene and waste water, which is applied in chemical instruments and methods, natural water treatment, water/sewage multi-stage treatment, etc., and can solve the requirements that nitrochlorobenzene is difficult to meet the discharge standard, lack of organic matter content reduction, The regeneration of the adsorption resin is difficult and other problems, and the treatment effect is stable and reliable, the content of organic pollutants is reduced, and the effect of easy industrial scale-up is achieved.
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Embodiment 1
[0025] The pH value of nitrochlorobenzene production wastewater in a company is 12.0, the salt content is 2.7%, the content of nitrochlorobenzene is 1180mg / L, and the chroma is 5000 times.
[0026] The temperature in the bottom of the stripper is controlled at 115°C, the pressure (gauge pressure) at the top of the stripper is controlled at 0.05MPa, the number of theoretical plates of the stripper is 25, and the outflow of the top of the stripper is 20% of the water entering the tower Under certain conditions, the content of nitrochlorobenzene in the effluent of the stripping tower can be reduced to within 30 mg / L.
[0027] Next, when the temperature of the waste water is 98° C., the pH of the effluent of the stripping tower is adjusted to 5.0 with 5% sulfuric acid.
[0028] Next, the wastewater is subjected to catalytic oxidation treatment, the temperature of the catalytic oxidation reaction system is controlled at 98°C, the pressure is normal pressure, and the amount of 27.5%...
Embodiment 2
[0031] The pH value of nitrochlorobenzene production wastewater from a company is 13.0, the salt content is 2.3%, the content of nitrochlorobenzene is 780mg / L, and the chroma is 4200 times.
[0032] Under the conditions that the temperature of the stripper tower kettle is controlled at 105°C, the stripper tower top pressure is controlled at normal pressure, the stripper theoretical plate number is 15, and the stripper tower top outflow is 10% of the water entering the tower, The content of nitrochlorobenzene in the effluent of the stripping tower can be reduced to less than 50mg / L.
[0033]Next, when the temperature of the waste water is 80° C., the pH of the effluent of the stripping tower is adjusted to 2.5 with 5% sulfuric acid.
[0034] Next, the wastewater is subjected to catalytic oxidation treatment, the temperature of the catalytic oxidation reaction system is controlled at 80°C, the pressure is normal pressure, and the amount of 27.5% hydrogen peroxide is added accord...
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