Method for cooperative remove of nitrate, ammonia nitrogen and COD in polluted water body
A technology of ammonia nitrogen and nitrate nitrogen is applied in the field of synergistic removal of nitrate nitrogen, ammonia nitrogen and COD in polluted water bodies, which can solve the problems of secondary pollution and low treatment efficiency, and achieve the effect of saving construction costs and floor space.
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Embodiment 1
[0021] The upflow fixed bed reactor consists of water inlet, heterotrophic aerobic reaction zone, hydroautotrophic anaerobic reaction zone and water outlet from bottom to top; the water inlet is connected to the water inlet pump through pipelines, and the DC power supply is connected to the hydrogen autotrophic anaerobic reaction zone through wires. The oxygen reaction zone is connected.
[0022] The hydrogen autotrophic anaerobic reaction zone consists of three-dimensional electrodes and fillers between the electrodes; a DC power supply is connected with the three-dimensional electrodes through wires. The anode of the three-dimensional electrode is a carbon rod, and the cathode is a stainless steel mesh; the stainless steel mesh is arranged on the upper part of the heterotrophic aerobic reaction zone; the filler is ordinary carbon particles, and its size is determined according to the size of the reactor.
[0023] Removal method:
[0024] The waste water to be treated is a r...
Embodiment 2
[0033] The waste water to be treated comes from a river in Weifang, Shandong. Due to the direct discharge of sewage in rural areas in recent years, the supervision of industrial waste water is unfavorable, the excessive application of chemical fertilizers, and the pollution is heavy. The COD value in the water is 300mg / L, and the NO 3 - -N value 60mg / L;
[0034] The above-mentioned cement ascending fixed bed reactor with a diameter of 1.5 meters and a height of 2.5 meters is constructed near the downstream of the river to be treated. The anode of the three-dimensional electrode in the reactor is a carbon rod with a diameter of 25 cm and a length of 30 cm; the cathode is a stainless steel mesh , the stainless steel mesh is cut into a diameter of 1.2m and fixed on the upper part of the heterotrophic aerobic reaction zone; the filler is ordinary carbon particles with a particle size of 2-5cm.
[0035] Specific process:
[0036] 1) Take aerobic sludge (reflux sludge from aeratio...
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