Dynamic micro-electrolysis waste water treatment device and water treatment method thereof
A technology for dynamic micro-electrolysis and wastewater treatment, applied in the field of water treatment, can solve the problems of unsolved problems such as oxygen deficiency in iron-carbon micro-electrolysis zone, feeding and slag discharge, difficulty in operation, and no iron-carbon feeding and slag discharge. , to achieve the effect of saving reaction space and raw materials, easy management and maintenance, convenient maintenance and cleaning
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Embodiment 1
[0022] Such as figure 1 and figure 2 As shown, this embodiment includes: drum reactor 1, water inlet pipe 2, air inlet pipe 3, outlet pipe 11, air outlet pipe 10, transmission belt 5, aeration pipe 7 and support base 14, wherein: drum reactor 1 is installed on On the support base 14 of the base 13, the driving motor 15 is fixed on the base 13 and the transmission shaft 12 of the driving motor 15 is connected with the transmission belt 5 and the drum reactor 1 in turn to realize the rolling of the drum reactor 1, and the both sides of the drum reactor 1 A sealed rotary interface 4 is provided and connected to the water inlet pipe 2, the air inlet pipe 3 and the water outlet pipe 11 and the air outlet pipe 10 respectively. connect.
[0023] The iron-carbon mixture is filled in the roller reactor 1, and the rolling of the roller reactor 1 is driven by the driving motor 15 to form a dynamic iron-carbon bed. The scraper 6 in the roller reactor 1 is conducive to the dispersion of...
Embodiment 2
[0028] The roller reactor 1 that adopts plexiglass to make by embodiment 1, the effective volume of roller reactor 1 is 10 liters, iron filings and gac (solid-to-liquid ratio 5: 8) are packed into, the COD6000mg / amantadine hydrochloride water of pH 1.0 Introduce into the drum reactor 1, feed water continuously, start the motor 15, drive the reactor to rotate, and aerate through the air inlet pipe 3; the waste water undergoes micro-electrolysis reaction in the drum reactor, and the residence time is controlled at 0.5 hours. The waste water is discharged through the water outlet 11; the waste water treated by the above method has a COD removal rate of 40%
Embodiment 3
[0030] The roller reactor 1 that adopts plexiglass to be made by embodiment 1, the effective volume of roller reactor 1 is 10 liters, iron filings and gac (solid-to-liquid ratio 5: 8) are packed into, the COD6000mg / amantadine hydrochloride water of pH 5.0 Introduce into the drum reactor 1, feed water continuously, start the motor 15, drive the reactor to rotate, and aerate through the intake pipe 3; the waste water is subjected to micro-electrolysis reaction in the drum reactor, and the residence time is controlled at 6 hours. The waste water is discharged through the water outlet 11; the waste water treated by the above method has a COD removal rate of 35%. The water treated by the drum-type iron-carbon micro-electrolysis reaction device is added with H2 o 2 3ml / L, Fenton oxidation for 20min, the COD removal rate increased by 10%.
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