Electro-Fenton composite oxidation device and method for degrading organic pollutants in high-chlorine-content sewage
A technology of organic pollutants and composite oxidation, which is applied in the direction of water pollutants, chemical instruments and methods, water/sewage treatment, etc., can solve the problems of complex preparation, easy loss of iron salt, and poor electrode recyclability, so as to increase biochemical Sexuality, COD reduction effect
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Embodiment 1
[0041] Such as figure 2 As shown, this embodiment provides an electric Fenton compound oxidation device for degradation of organic pollutants in high chlorine-containing sewage, the device is a plate-and-frame electrolyzer without a diaphragm, and the plate-and-frame electrolyzer without a diaphragm includes a shell Body 5, anode 2, cathode 1, water inlet 3, water outlet 4 and aeration tube 6, the anode 2 is a ruthenium iridium titanium electrode, the cathode 1 is a gas diffusion electrode, and the gas diffusion electrode includes: a catalytic layer , current collector and diffusion layer; the material used in the catalytic layer is carbon nanotube; the current collector is titanium mesh; the material used in the diffusion layer is polytetrafluoroethylene. Both the anodes 2 and the cathodes 1 are four, and are alternately arranged in a plate-and-frame electrolytic cell without a diaphragm. The aeration pipe 6 is arranged at the bottom of the plate-and-frame electrolytic cell...
Embodiment 2
[0043] This embodiment provides a method for electro-Fenton composite oxidation for the degradation of organic pollutants in high-chlorine sewage. The device of complex oxidation, the high chlorine-containing sewage used in the present embodiment is dye waste water, and the present embodiment comprises the following steps:
[0044] Pass the dye wastewater into the plate-and-frame electrolytic cell without a diaphragm, the flow rate of the dye wastewater is 10L / h, start the constant-current stabilized power supply, and set the current density to 10mA / cm 2 , using the aeration pipe 6 to feed air into the device to degrade the dye wastewater. The air-to-water ratio of the amount of air that the aeration pipe 6 feeds into the plate-and-frame electrolytic cell without a diaphragm to the amount of dye wastewater in the plate-and-frame electrolytic cell without a diaphragm is 1:10. The reaction conditions of the degradation treatment are alkaline conditions with a pH of 9. The chlo...
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