Method for removing COD (chemical oxygen demand) and ammonia nitrogen from wastewater by using titanium-base lead peroxide composite electrode
A composite electrode and lead dioxide technology, applied in chemical instruments and methods, oxidized water/sewage treatment, water/sewage treatment, etc., can solve the problems of reducing the efficiency of electro-oxidation current, easily generating oxygen and chlorine, and reduce the cost , reduce processing costs, and simplify the effect of connecting lines
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[0043] Example 1
[0044] The biochemical effluent treatment of a fine chemical plant, the realization method:
[0045] The actual electrolytic cell diagram is as Figure 1-Figure 4 As shown,
[0046] The electrolytic cell uses titanium-based lead dioxide composite electrode plates as both anode and cathode plates. The composite electrode plates are arranged in sequence to form a number of cell units. The anode and the cathode of the adjacent composite electrode plates are opposed to each other, and 7 composite electrodes are spaced apart. The plate is provided with a baffle with a gap left on the wall of the electrolytic cell, and every two adjacent baffles are staggered with the gap left on the wall of the electrolytic cell. A water inlet is provided above one end of the electrolytic cell, and the other end A water outlet is provided below the composite electrode plate, the composite electrode plate is made of a titanium-based lead dioxide anode plate and a titanium plate cathode...
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[0050] Example 2:
[0051] The electrolytic cell is the same as in Example 1, and the distance between the adjacent composite electrode plates is changed to 2 cm.
[0052] The water quality of the biochemical tail water of a textile printing and dyeing company is: conductivity 14.33ms / cm, salinity 7.36g / L, ammonia nitrogen 162mg / L, pH6.8, COD 650mg / L, color 500. The wastewater treatment process is the same as in Example 1, and the results are shown in Table 2.
[0053] Table 2 Water quality before and after treatment of printing and dyeing wastewater
[0054]
[0055] The results of Table 1 and Table 2 show that the current density is 15mA / cm 2 Under the suitable treatment conditions, the wastewater has a hydraulic retention time of 1h, and the effluent COD and ammonia nitrogen can both meet the nanotube standard. The electrocatalytic oxidation method involved in the present invention is suitable for the advanced treatment of industrial wastewater biochemical effluent.
[0056] In summ...
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