Wastewater treatment method based on electro-Fenton reaction
A wastewater treatment and reaction technology, applied in water/sewage treatment, oxidized water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of high cost and many by-products, prolong service life and reduce side effects. product, the effect of improving the reaction efficiency
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Embodiment 1
[0021] The concentration of treatment is 40mg / L, the volume is 300mL of methylene blue and Congo red organic dye aqueous solution, the pH value of the system is not adjusted, wherein the pH of methylene blue aqueous solution is 6.35, and the pH of Congo red aqueous solution is 6.97. The anode and cathode are 40-mesh SUS 304 stainless steel mesh. Adjust the concentration of sodium sulfate electrolyte to 3g / L, and pass air into it for aeration. Turn on the DC power supply to control the current to 0.6A, and time the response. See Table 1 for the treatment effect
[0022] time (h)
1
2
Methylene blue (removal rate)
92%
99.7%
Congo red (removal rate)
84.8%
95.5%
[0023] Table 1
[0024] It can be seen from Example 1 that at about neutral pH, the electro-Fenton reaction can efficiently treat organic wastewater, and the effect is obvious.
Embodiment 2
[0026] The treatment concentration is 20mg / L, the volume is the methylene blue aqueous solution of 300mL, investigates the reaction effect of adjustment and unadjusted system pH respectively, when unadjusted intrinsic pH6.50, adjust the pH3.00 of system with hydrochloric acid solution; Anode and The cathode is an 80-mesh stainless steel mesh of SUS 304. Adjust the concentration of sodium sulfate electrolyte to 3g / L, and pass air into it for aeration. Turn on the DC power supply to control the current to 0.3A, and time the response. See Table 2 for the treatment effect
[0027] time (h)
1
2
Methylene blue pH6.50 (removal rate)
66.5%
92.8%
Methylene blue pH3.00 (removal rate)
99.8%
[0028] Table 2
[0029] As can be seen from Example 2, the efficiency of the electrochemical reaction is higher under acidic pH conditions, this is because the hydroxyl radical reaction of the Fenton reaction under acidic pH is dominant, ...
Embodiment 3
[0031] The treatment concentration is 40mg / L, and the volume is 300mL of methylene blue aqueous solution, and the effects of using stainless steel mesh and stainless steel plate with different meshes as reaction cathode and anode are respectively investigated. The pH of the system was not adjusted. Adjust the concentration of sodium sulfate electrolyte to 3g / L, introduce air for aeration, and time the reaction. For the treatment effect, see
[0032] table 3
[0033] time (h)
1
2
Methylene blue (removal rate) electrode: mesh number
40 mesh stainless steel mesh
80%
94.5%
Methylene blue (removal rate) electrode: mesh number
80 mesh stainless steel mesh
95%
99.4%
Methylene blue (removal rate) electrode: stainless
steel plate
72.3%
95%
[0034] table 3
[0035] It can be seen from Example 3 that with the increase of the mesh number of stainless steel, the removal efficiency of ...
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