Electrochemical biological combined denitrification reactor
A technology of electrochemical biology and reactor, which is applied in chemical instruments and methods, sustainable biological treatment, biological water/sewage treatment, etc. It can solve the problems of uncontrollable denitrification intensity, achieve small footprint and avoid sludge Expansive, compact and simple effect
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Embodiment 1
[0014] An electrochemical biological combined denitrification reactor, such as figure 1 , 2 As shown, it includes a cell body 1, an electrode, a modified activated carbon particle electrode 9, an aeration device 8 and a steady current transformer 7. The two ends of the cell body 1 are respectively provided with a water inlet 2 and a water outlet 4; the electrodes include an anode 5 and a cathode 3, the anode 5 is arranged in the center of the cell body 1, and the cathode 3 surrounds the anode 5 and is arranged near the cell wall. The material used for the anode 5 is a titanium plate, and the material used for the cathode 3 is graphite; the anode 5 and the cathode 3 are respectively connected to the positive and negative poles of the steady current transformer 7; the spherical modified activated carbon particle electrode 9 is filled between the anode 5 and the cathode 3; The aeration device includes a microporous aerator 6 arranged at the bottom of the pool body 1 and an air p...
Embodiment 2
[0017] The structure of the reactor is the same as in Example 1, the anode 5 is made of titanium-based lead dioxide-plated material, and the cathode 3 is made of stainless steel. Processing flow is the same as embodiment 1.
[0018] Using a complex three-dimensional electrode-biofilm reactor with a titanium-based lead dioxide-plated material as the anode and a stainless steel cathode as the direct treatment of COD to 45mg / L, NH 3 -N=30mg / L, TN is 40mg / L simulated wastewater, under the conditions of T=28℃, DO=1.2mg / L, HRT=8h, I=25mA, the effluent COD is 30mg / L, TN=3.2mg / L, NH 3 - N = 1.9 mg / L.
Embodiment 3
[0020] The structure of the reactor is the same as in Example 1, the anode 5 is made of titanium-based ruthenium dioxide plated plate material, and the cathode 3 is made of graphite material. Processing flow is the same as embodiment 1.
[0021] Using a complex three-dimensional electrode-biofilm reactor with a titanium-based ruthenium dioxide-coated material as the anode and a graphite material as the cathode, the COD is 45mg / L and NH is directly processed. 3 - Simulated wastewater with N=30mg / L and TN of 40mg / L was carried out under the same conditions as Case 2: T=28°C, DO=1.2mg / L, HRT=8h, I=25mA, and the effluent COD was 26mg / L, TN=1.1mg / L, NH 3 - N = 0.82 mg / L.
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