Method and device used for processing nitrochlorobenzene production wastewater
A technology for the production of nitrochlorobenzene and waste water, which is applied in natural water treatment, chemical instruments and methods, heating water/sewage treatment, etc., and can solve the problem that nitrochlorobenzene is difficult to meet discharge standards, adsorption resin regeneration is difficult, tetrachlorination Carbon problems and other issues, to achieve stable treatment effect, easy industrial scale-up, and small footprint
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Embodiment 1
[0049] The pH value of nitrochlorobenzene production wastewater in a company is 12.0, the salt content is 2.7%, the content of nitrochlorobenzene is 1100mg / L, and the chroma is 5000 times.
[0050] When the operating temperature of the stripper is 115°C, the pressure (gauge pressure) at the top of the stripper is controlled at 0.05MPa, and the theoretical plate number of the stripper is 25, when the outflow of the top of the stripper is 20% of the water entering the tower Under these conditions, the content of nitrochlorobenzene in the effluent of the stripping tower can be reduced to below 30 mg / L.
[0051] Next, under the condition that the wastewater temperature is 40°C, the wastewater is subjected to photo-assisted Fenton catalytic oxidation treatment. Use 98% sulfuric acid to adjust the pH of the wastewater to 2.5, use 27.5% hydrogen peroxide as the oxidant, and add hydrogen peroxide at 4g per L of wastewater, use ferrous sulfate as the catalyst, and use ferrous salt at 8...
Embodiment 2
[0054] The pH value of a company's nitrochlorobenzene production wastewater is 13, the salt content is 2.3%, the nitrochlorobenzene content is 780 mg / L, and the chroma is 4200 times.
[0055] Under the condition that the operating temperature of the stripper is 105°C, normal pressure, and the number of theoretical plates of the stripper is 10, and the outflow from the top of the stripper is 10% of the water entering the tower, the effluent water from the bottom of the stripper The content of nitrochlorobenzene can be reduced to below 50mg / L.
[0056] Next, under the condition that the wastewater temperature is 50°C, the wastewater is subjected to light-assisted Fenton catalytic oxidation treatment. Use 98% sulfuric acid to adjust the pH of the wastewater to 3.0, use 27.5% hydrogen peroxide as the oxidant, add the amount of hydrogen peroxide at 3g per L of wastewater, use ferrous sulfate as the catalyst, and use 100mg Fe per L of wastewater 2+ For dosing, the light source is a...
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