Method for treating sewage of circulating cooling water in renewable water resource
A technology of circulating cooling water and treatment methods, applied in the directions of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., can solve the problems such as difficulty in meeting discharge requirements to achieve elimination of adverse effects, Improve denitrification efficiency and denitrification effect
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Embodiment 1
[0029] During the treatment process of regenerated water source circulating water and sewage in a thermal power plant, the influent CODcr is 80-150mg / L, ammonia nitrogen is 8-15mg / L, total nitrogen is 30-50mg / L, and total phosphorus is 1.5-3.5mg / L . The wastewater enters the self-cleaning filter after adjusting the water volume and quality in the regulating tank, and the effluent from the self-cleaning filter enters the ozone oxidation pool from the upper part. The Kongbu air cap diffuses into the wastewater and fully contacts with the wastewater countercurrently. The dosage of ozone is 15mg / L, the hydraulic retention time is 30min, and an ozone tail gas destroyer is installed on the top of the pool. The effluent from the ozone oxidation pool enters the buffer pool for a residence time of 45 minutes. The effluent from the buffer pool enters the aerobic pool, and biological ropes are placed in the pool. The material is vinylon, the outer diameter is 30mm, the filling ratio is ...
Embodiment 2
[0032] During the treatment process of regenerated water source circulating water and sewage of a thermal power plant, the influent CODcr is 100-200mg / L, ammonia nitrogen is 10-18mg / L, total nitrogen is 30-65mg / L, and total phosphorus is 1.5-5mg / L. The wastewater enters the self-cleaning filter after adjusting the water volume and quality in the regulating tank, and the effluent from the self-cleaning filter enters the ozone oxidation pool from the upper part. The Kongbu gas cap diffuses into the wastewater and fully contacts with the wastewater countercurrently. The dosage of ozone is 20mg / L, the hydraulic retention time is 40min, and an ozone tail gas destroyer is installed on the top of the pool. The effluent from the ozone oxidation pool enters the buffer pool for a residence time of 50 minutes. The effluent from the buffer pool enters the aerobic tank, and biological ropes are placed in the pool, made of vinylon and polypropylene, with an outer diameter of 45mm, a filling...
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