A device for treating nitrobenzene wastewater
A technology for nitrobenzene and wastewater, which is applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, water pollutants, etc. Equal problems, to achieve the effect of improving ozone utilization, improving treatment efficiency, and simple process flow
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Embodiment 1
[0041] Example 1: Treatment of dinitrotoluene (DNT) in waste water from a propellant and explosive factory. The initial concentration of dinitrotoluene in the wastewater is 190mg / L. Micro-electrolysis is used to treat 2.5L of wastewater. At pH=3, the amount of iron powder added is 28g / L, and the mass ratio of iron to carbon is Fe:C=1:1. The reaction time is 1.5h, and the stirring speed of the stirrer is 200r / min, more than 80% of the nitro compounds are converted into aniline substances, and the liquid-gas volume ratio of the micro-electrolyzed water and ozone is 400L / m 3 , the ozone concentration is 50mg / L, the rotation speed of the rotating packed bed is 500rpm, and after 60 minutes of degradation, the pollutant removal rate is over 98%; while the wastewater without micro-electrolysis pretreatment has the same treatment capacity and ozone concentration The removal rate of its nitro compounds is only 50%. Micro-electrolysis pretreatment can significantly improve the biodegra...
Embodiment 2
[0042] Embodiment 2: Treatment of TNT wastewater. The concentration of trinitrotoluene in the waste water is 16 mg / L, and the pH value is adjusted to 3.0 with dilute sulfuric acid. Take 2L of water samples, and use micro-electrolysis to pretreat the wastewater. The amount of iron powder added is 10g / L, the mass ratio of iron to carbon is 1:1.5, the stirring speed is 400r / min, and the reaction time is 1.5h. More than 100% of nitro compounds are converted into aniline substances, and the liquid-gas ratio of micro-electrolysis water and ozone is 100L / m 3 , the ozone concentration is 25mg / L, the height of the rotating packed bed is 18cm, the diameter is 12cm, and the rotation speed is 1200rpm. After 30 minutes of reaction, the removal rate of organic pollutants in wastewater is almost 100%. However, the micro-electrolysis / ozone process has a pollutant removal rate of only about 40% when the liquid-gas ratio, ozone concentration, stirring speed, and reaction time are constant %, ...
Embodiment 3
[0043] Embodiment 3: Treatment of nitrobenzene wastewater. The concentration of nitrobenzene in the wastewater is 100mg / L, and the pH value is adjusted to 1.5. Take 3.5L of water sample, and use micro-electrolysis to pretreat p-nitrobenzene wastewater. The reaction time is 1h, the stirring speed is 600r / min, the iron powder addition is 20g / L, and the iron-carbon mass ratio is 3:1. , the reduction rate is over 96%, and the liquid-gas ratio of micro-electrolysis water and ozone is 50L / m 3 , the ozone concentration is 40mg / L, the height of the rotating packed bed is 18cm, the diameter is 12cm, and the rotation speed is 2000rpm. After 1 hour of reaction, the removal rate of organic pollutants in wastewater is almost 100%. Under the conditions of the same liquid-to-gas ratio, ozone concentration and reaction time, the removal rate of nitro compounds is only 20%. The micro-electrolysis / ozone process has a pollutant removal rate of about 50% when the liquid-gas ratio, ozone concent...
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