Treatment method for phenol and cyanide wastewater generated by gas producer
A technology of gasifier and treatment method, which is applied in biological water/sewage treatment, neutralized water/sewage treatment, multi-stage water/sewage treatment, etc. It can solve the problem of unstable treatment effect of biochemical treatment methods and the preparation of coal water slurry Large system investment, high processing cost and other issues, to achieve obvious economic and environmental benefits, avoid inhibition, and reduce pollution
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Embodiment 1
[0007] Example 1: Treat 1m per day 3 Phenol cyanide wastewater (pH8.2, COD Cr 8500mg / L, volatile phenol 910mg / L, CN - 4.2mg / L, T-N115mg / L), after reduction with aluminum-zinc composite powder (add 5g of aluminum-zinc composite powder per liter of wastewater, time 4h, 25°C, CO 2 Pressure 0.1MPa), hydrolytic acidification (24h, pH6.0), aerobic biochemical (12h) and activated carbon biological filter tower (hydraulic load is 40m 3 / m 2 .d, the total thickness of activated carbon is 2m) treatment, the effluent water quality is COD Cr 82mg / L, CN - 0.18mg / L, volatile phenol 0.37mg / L, T-N 18mg / L.
Embodiment 2
[0008] Embodiment 2: 20m is processed every day 3 Phenol cyanide wastewater (pH8.3, COD Cr 8000mg / L, volatile phenol 860mg / L, CN - 3.9mg / L, T-N101mg / L), after reduction with aluminum-zinc composite powder (add 10g of aluminum-zinc composite powder per liter of wastewater, time 2h, 45°C, CO 2 Pressure 0.3MPa), hydrolytic acidification (8h, pH8.0), aerobic biochemical (8h) and porous ceramsite biological filter tower (hydraulic load is 100m 3 / m 2 .d. The total thickness of porous ceramsite is 4m), and the effluent quality is COD Cr 70mg / L, CN - 0.10mg / L, volatile phenol 0.27mg / L, T-N 16mg / L.
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