Method for treating waste water containing sulfuric acid in production process of dyes and intermediates
A production process and wastewater treatment technology, which is applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., to achieve the effects of stable operation, high degree of automation, and few supporting facilities
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[0043] Example 1
[0044] Process flow chart such as figure 1 As shown, the waste water containing sulfuric acid (taken from the mother liquor of the disperse blue 291:4 and the disperse violet 93:4 production process is mixed, the acidity of sulfuric acid is about 3%, the color is 750 times) is pumped into the decolorization kettle, and the quality of the waste water is added. 2.5% activated carbon adsorption decolorization, the decolorization temperature is controlled at 45℃~50℃, keep for 3 hours, sample and filter, the filtrate has 9 times the color, and the decolorization is over. Filter and separate to obtain decolorized waste water and activated carbon residue, pump the decolorized waste water into the adsorption kettle, add 3% polyacrylamide of the decolorized waste water mass, control the temperature at 30℃~35℃, keep it for 1 hour, filter to obtain adsorption waste residue and The adsorbed wastewater is pumped into the neutralization kettle, and neutralized with 30% liqu...
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[0046] Example 2
[0047] Pump sulfuric acid-containing wastewater (taken from the mother liquor of Disperse Blue 291:4 production process, sulfuric acid acidity is about 9%, and chroma 700 times) into the decolorization kettle, start stirring and add 1% of sulfuric acid-containing wastewater mass for decolorization and decolorization temperature Control at 20℃~25℃, keep for 1 hour, sample and filter, the color of the filtrate is 8 times, and the decolorization is over. Filter and separate to obtain decolorized waste water and activated carbon residue, pump the decolorized waste water into the adsorption kettle, add 0.05% EDTA of the decolorized waste water mass, control the temperature at 20℃~25℃, keep for 5 hours, filter to obtain the adsorption waste residue and after adsorption Wastewater: Pump the adsorbed wastewater into the neutralization kettle, neutralize it with flake caustic soda (sodium hydroxide solid) to a pH of about 7-8, filter and separate to obtain sodium sulfat...
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[0049] Example 3
[0050] Pump sulfuric acid-containing wastewater into the decolorization tank (taken from the mother liquor water of the Disperse Red FBS production process, sulfuric acid acidity is about 16%, and color is 900 times), start stirring and add 5% of sulfuric acid-containing wastewater mass to decolorize, and control the decolorization temperature Incubate at 65℃~70℃ for 5 hours, sample and filter, the color of the filtrate is 22 times, filtered and separated to obtain decolorized waste water and activated carbon residue. After decolorization, the waste water is pumped into the adsorption kettle, and 5% hexametaphosphoric acid is added to the decolorized waste water. Sodium, the temperature is controlled at 45℃~50℃, keep for 5 hours, filter the adsorbed waste residue and adsorbed waste water, add 30% hydrogen peroxide to the adsorbed waste water for oxidation, the amount of hydrogen peroxide is 0.1% of the quality of the adsorbed waste water, and the oxidation tempe...
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