A method for treating wastewater by adding hydrogen peroxide to the electric Fenton
A technology for treating wastewater and sewage, which is applied in the field of electro-Fenton treatment of wastewater with H2O2 added, and can solve the problems of unfavorable Fenton reaction, limited removal efficiency of organic matter, and low electro-Fenton treatment efficiency.
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Embodiment 1
[0053] Take reverse osmosis concentrated water from a petrochemical company, its COD Cr It is 60.20~82.77mg / L, the turbidity is 1.12~3.15NTU, and the conductivity is 9020~9150μS / cm.
[0054] according to figure 1The process shown is for treatment, but does not include screen filtration, water quality and quantity adjustment, and sludge thickening and dewatering processes. The anode is made of iron plate, the cathode is made of stainless steel plate, through 1mol / L H 2 SO 4 The solution is adjusted to obtain acidic wastewater with pH=4;
[0055] The experimental power supply adopts constant current mode, and the current density is 10mA / cm 2 , the acidic wastewater flows through the reactor at a flow rate of 0.5m / s, and H is added to the source of the acidic wastewater 2 o 2 , so that the H in the acidic wastewater at the source 2 o 2 The concentration is 150mg / L, and air is introduced into the system through aeration at the same time. The hydraulic retention time in th...
Embodiment 2
[0068] The secondary sedimentation effluent of paper deinking wastewater from a paper mill was taken, and its COD was determined cr It is 451.4~511.6mg / L.
[0069] It is processed by the same device as in Example 1, the anode adopts an iron plate, and the cathode adopts a stainless steel plate, and the H of 1mol / L 2 SO 4 The solution is adjusted to obtain acidic wastewater with pH=4.
[0070] The experimental power supply adopts constant current mode, and the current density is 10mA / cm 2 , Acidic waste water flows through the reactor at a flow rate of 0.5m / s. Dosing H at the source of acidic wastewater 2 o 2 , such that at the source H 2 o 2 The concentration is 300mg / L. At the same time, oxygen is introduced into the system through aeration. The aeration rate is 2000mL / (L min). The hydraulic retention time in the Fenton reaction tank is 30min;
[0071] After the reaction, the wastewater was settled in the sedimentation tank for 30 minutes, and the supernatant was tak...
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