Method and equipment for mineralizing and degrading organic wastewater
A technology for organic wastewater and organic compounds, which is applied in light water/sewage treatment, oxidized water/sewage treatment, added substance water/sewage treatment, etc. problem, to achieve the effect of low cost, low maintenance cost and few processing units
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Embodiment 1
[0033] The wastewater treated in this embodiment is an aqueous solution containing dinitrotoluene, and the content of dinitrotoluene is 30 mg / L. Select 1.5 grams of nanoscale platinum and 10 mL of hydrogen peroxide, and treat 2 liters of wastewater. First, waste water is added to the treatment equipment through the water inlet pipe 14, and then the catalyst is added into the waste water through the water inlet pipe 14; the air pump 10 is started, the light source is turned on to make the quartz tube and the ultraviolet lamp 5 emit light; the organic matter in the waste water begins to be degraded, and the waste gas is discharged from the top pipe discharge. Take a water sample at regular intervals, such as every 20 minutes, and measure the content of dinitrotoluene with a high-performance liquid chromatograph. After the COD reaches the standard, the treated water is discharged from the drain pipe 8 and valve 7 at the bottom. The content of dinitrotoluene after treatment was ...
Embodiment 2
[0035] The wastewater treated in this embodiment is the same dinitrotoluene-containing aqueous solution as in Example 1, and the content of dinitrotoluene is 30 mg / L. 1.5 grams of nano-scale silver and 10 mL of hydrogen peroxide are selected to treat 2 liters of waste water. Processing method is identical with embodiment 1.
[0036] The content of dinitrotoluene after treatment was 1.4mg / L. The results show that the catalytic system can effectively degrade dinitrotoluene, and make the content of dinitrotoluene in water lower than the emission standard stipulated by the state.
Embodiment 3
[0038] The wastewater treated in this embodiment is the same dinitrotoluene-containing aqueous solution as in Example 1, and the content of dinitrotoluene is 30 mg / L. A combination of 1.5 grams of nano-scale silver and ozone is used as a catalyst, and the amount of wastewater treated is 2 liters. Processing method is identical with embodiment 1.
[0039] The content of dinitrotoluene after treatment was 3.6mg / L. The results show that the catalytic system can effectively degrade dinitrotoluene, and the content of dinitrotoluene in water is lower than the national emission standard.
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