The wastewater treatment system using denitrification apparatus by the electrolytic method was developed. The bench-scale-size system which capacity is 1~2 m3/day and tank volume is 55 L, was produced by experiment. The conversion of nitrate ion, nitrite ion and ammonium ion to nitrogen gas was 90% after 60 minutes of reaction. The concentration of nitrate ion, nitrite ion and ammonium ion in the initial reaction solution was 1860 mg L−1, 330 mg L−1 and 540 mg L−1 (Total-N 900 mg L−1). In this method, the highly-activated electrodes were used as a Cu-Zn cathode and a Pt/Ru/Ti anode. The main electrolytic reaction of nitrate removal involved cathodic reduction of NO3− to NH3 (NO3− + 6H2O + 8e → NH3 + 9OH−) and anodic oxidation of Cl− to HClO (2Cl− → Cl2 + 2e−, Cl2 + H2O → HClO + HCl), and finally got N2 by redox reaction (2NH3 + 3HClO → N2 ↑ + 3HCl + 3H2O). Ampholyte element (Al, Zn) contributed to the rise of cathodic reduction. The performance of denitrification apparatus was analyzed by the measured data. As a result, it was concluded that the power consumption for denitrification was 20≫60 kWh/kg-N by this method.
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