Integrated electrochemical reaction apparatus for processing difficultly degraded organic waste water and processing method thereof
A technology for organic wastewater treatment and chemical reaction, applied in chemical instruments and methods, water/sewage treatment, water/sludge/sewage treatment, etc., which can solve the problems of single treatment of pollutants, limited use, low current efficiency and utilization rate, etc. , to achieve the effect of speeding up the reaction process, increasing the rate and good treatment effect
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[0038] Example 1
[0039]The refractory organic waste water is injected into the reactor shell 10 through the water inlet pipe 2; the regulated power supply 11 and the starter motor 1 are turned on, the current is 5A, the output speed of the motor 1 through the reducer 14 is 1.5 rpm, and the stainless steel cathode 6 Under the driving of the motor 1, it rotates slowly, and the waste water is slowly stirred, so as to increase the molecular collision in the reaction process and improve the reaction efficiency; wherein, in the vicinity of the semi-arc ruthenium-iridium anode 9, electricity occurs in the chlorine-containing waste water. The oxidation process effectively removes ammonia nitrogen in wastewater, and the generated hypochlorous acid oxidant has both disinfection effect on wastewater, and at the same time, the nitrogen gas produced has no secondary pollution; the semi-arc porous iron mesh 3 is used as the anode used in parallel, and the external power supply Under the a...
Example Embodiment
[0040] Embodiment 2
[0041] According to the operation steps of the first embodiment, the wastewater of the reactor shell 10 comes from the leachate of an aging landfill. The aging landfill leachate has high pollution, large fluctuation time of water quality and poor biodegradability. The integrated electrochemical reaction device can be used as a treatment device in the pretreatment process to remove some pollutants in the wastewater, improve the biodegradability of the wastewater, and facilitate subsequent biochemical treatment. The current of the reaction device is 5A, the residence time of the waste liquid is 5h, and the measured average influent COD, ammonia nitrogen and TP concentrations are 3000, 240 and 30 mg / L, respectively. Under the action of various mechanisms, the average effluent COD, ammonia nitrogen and The TP concentrations were 468, 47 and 3.2 mg / L, respectively, and the removal rates of COD, ammonia nitrogen and TP were 84%, 80%, and 88%, respectively, and ...
Example Embodiment
[0042] Embodiment 3
[0043] According to the operation steps of the first embodiment, the influent of the wastewater in the reactor shell 10 comes from the wastewater discharged from a coking plant. The coking wastewater has complex components. In addition to high concentrations of inorganic substances such as ammonia nitrogen and cyanide, it also contains a large amount of Phenols, pyridine, quinoline and other toxic and refractory organic pollutants. This integrated electrochemical reaction device is used for coking wastewater treatment, and the influent condition is COD 3500mg / L, of which volatile phenol is 640mg / L and ammonia nitrogen is 280mg / L. Set the reaction current to 5A and the residence time to 8h. After the action of the reactor, the average effluent COD is 600mg / L, the volatile phenol content is reduced to 28mg / L, and the ammonia nitrogen concentration is 21mg / L. The yellow-black sediment produced during the reaction is discharged from the sludge discharge pipe...
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