Fenton reaction method for recycling iron-based catalyst
An iron-based catalyst and Fenton reaction technology, applied in chemical instruments and methods, water treatment of special compounds, oxidized water/sewage treatment, etc. Insufficient and other problems, to achieve the effect of reducing the amount of by-product sludge, reducing secondary pollution, and alleviating the intensity of treatment
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Embodiment 1
[0032] See figure 1 , In this embodiment, Fenton is used to pretreat disperse dye wastewater, which contains diphenylamine and o-aniline substances, which are refractory toxic wastewater. The Fenton treatment of wastewater controls the pH at 3.5-4 by adding sulfuric acid, the dosing ratio of ferrous sulfate is 6‰, the ratio of ferrous iron and hydrogen peroxide is 5:1, and the COD before Fenton treatment is 2500-3000mg / L, After Fenton treatment, the COD is reduced by 700-800mg / L, and the generated sludge is dehydrated by high-pressure diaphragm filter press. The amount of sludge per ton of aquatic products is 10-15kg, and the moisture content of the sludge is 60%.
[0033]Transform the original Fenton treatment system into an iron-based catalyst recycling Fenton reaction system. The pH of the iron-based catalyst recycling Fenton reaction pool 1 is controlled at 3.5 to 4. 1 Iron-based catalyst recycling Fenton reaction pool 1 does not need to pass through Sulfuric acid is add...
Embodiment 2
[0036] Please refer to Figure 2. In this embodiment, advanced treatment is performed on the tail water after sewage treatment to reduce COD from 80mg / L to 40mg / L. The iron-based catalyst is recycled and the pH of the Fenton reaction cell 1 is controlled at 4-4.5. The ferrous sulfate added in the Fenton reaction tank 1 is 0.04‰, the ratio of ferrous iron and hydrogen peroxide is 5:1, and the effluent after the Fenton reaction is adjusted to pH in the collection tank 2 by adding alkali. 7.5 to 8, ferric hydroxide precipitation is produced, pumped into the concentration device 3 for mud-water separation, the moisture content of the sludge through the concentration device 3 drops from 98% to 95%, and the separated supernatant enters the safety pool 7, Adding 30% sulfuric acid to the concentrated sludge in the acid-dissolving device 4 reduces the pH of the acid-dissolving device 4 to 3.0, and the ferric hydroxide floc disappearing solution is transparent yellow-brown. In the chemi...
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