A method and device for treating high-concentration nitrobenzene-containing wastewater by stripping-micro-electrolysis-fenton oxidation
A nitrobenzene wastewater, high-concentration technology, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc. and other problems, to achieve the effect of reducing the cost of water treatment, improving the oxidation efficiency and shortening the reaction time.
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Embodiment 1
[0050] Example 1: Using figure 1 The flow shown is for the treatment of wastewater containing nitrobenzene. The concentration of nitrobenzene in the water sample was 600mg / L, the pH value was 2.5, and the biochemical coefficient was only 0.1. The inner diameter of the supergravity reactor packing is 40 mm, the outer diameter is 75 mm, and the rotation speed is 1200 rpm. During the stripping process, the waste water flow rate is 25 L / h, and the gas-liquid ratio of fresh air and waste water in the supergravity equipment is 0.8 m 3 / L, the mass transfer rate of nitrobenzene from the liquid phase to the gas phase is increased by 2 times compared with the traditional method. When the concentration of nitrobenzene in the wastewater is 100 mg / L, the stripping time is reduced by 50% compared with conventional air stripping. At this time, micro-electrolysis is used to treat 2.0 L of wastewater, and the pH is adjusted to 3 with dilute hydrochloric acid. The amount of powder added is ...
Embodiment 2
[0051] Example 2: Using figure 1 The procedure shown treats a water sample containing nitrobenzene at a concentration of 800 mg / L. The inner diameter of the supergravity reactor packing is 30 mm, the outer diameter is 60 mm, and the rotation speed is 900 rpm. During the stripping process, the waste water flow rate is 35 L / h, and the gas-liquid ratio of fresh air and waste water in the supergravity equipment is 0.4 m 3 / L, the mass transfer rate of nitrobenzene from the liquid phase to the gas phase is increased by 2 times compared with the traditional method. When the concentration of nitrobenzene in the wastewater is 100 mg / L, the stripping time is reduced by 60% compared with conventional air stripping. At this time, the wastewater is passed into the micro-electrolyzer, and the pH value is adjusted to 2.0 with dilute sulfuric acid. Take 2L of water sample, and use micro-electrolysis to pretreat the wastewater. The amount of iron powder added is 10g / L, the mass ratio of iro...
Embodiment 3
[0052] Example 3: Using figure 1 The procedure shown treats a water sample containing nitrobenzene at a concentration of 900 mg / L. The inner diameter of the supergravity reactor packing is 0.6 m, the outer diameter is 1.4 m, and the rotation speed is 300 rpm. During the stripping process, the waste water flow rate is 25 L / h, and the gas-liquid ratio of fresh air and waste water in the supergravity equipment is 0.6 m 3 / L, the mass transfer rate of nitrobenzene from the liquid phase to the gas phase is 1.5 times higher than that of the traditional method. When the concentration of nitrobenzene in the wastewater is 80 mg / L, the stripping time is reduced by 60% compared with conventional air stripping. At this time, micro-electrolysis is used to pretreat 1.5L of wastewater, and dilute sulfuric acid is used to adjust the pH to 2.5. The amount of iron powder added is 30g / L, the mass ratio of iron to carbon Fe:C=1:1, the reaction time is 15 min, and the stirring speed of the stirr...
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