Treatment method of synthetic pharmacy organic wastewater
A technology of organic wastewater and treatment methods, which is applied in multi-stage water treatment, water/sewage treatment, natural water treatment, etc. It can solve the problems of high COD concentration of pollutants, difficulty in stably meeting discharge standards, and high cost of non-treatment, so as to reduce carbon Emissions, obvious economic and environmental benefits, and the effect of reducing treatment costs
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Embodiment 1
[0007] Embodiment 1: Treat 1m every day 3 Synthetic pharmaceutical organic wastewater (components: pH6.3, COD Cr 8400 mg / L, T-N39.3 mg / L, T-P33.3mg / L, chroma 230), reduced by iron-aluminum-manganese composite powder (1h, 40℃, CO 2 Pressure 0.6MPa, adding 20g of iron-aluminum-manganese composite powder per liter of wastewater), anaerobic (pH8.2, 72h, 25℃~35℃), aerobic (12h) and biological filter tower (total thickness of porous ceramsite packing layer 4m , hydraulic load 35m3 / m2.d) COD of effluent after treatment Cr It is 57mg / L, T-N8.1mg / L, T-P0.2mg / L, chroma 12.
Embodiment 2
[0008] Embodiment 2: Treat 25m every day 3 Synthetic pharmaceutical organic wastewater (components: pH5.7, COD Cr 5500 mg / L, T-N32.5 mg / L, T-P24.1mg / L, chroma 300), reduced by iron-aluminum-manganese composite powder (3h, 25℃, CO 2 Pressure 0.1MPa, adding 5g of iron-aluminum-manganese composite powder per liter of waste water), anaerobic (pH6.8, 24h, 35℃~55℃), aerobic (6h) and biological filter tower (total thickness of activated carbon packing layer 2m, hydraulic Load 90m 3 / m 2 .d) COD of effluent after treatment Cr It is 45mg / L, T-N / 7.6mg / L, T-P0.2mg / L, chromaticity 10.
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