Method for treating phenol and cyanide wastewater generated by gas producers
A technology of gas generator and treatment method, which is applied in biological water/sewage treatment, water/sewage treatment, water treatment parameter control, etc., can solve the problem of unstable treatment effect of biochemical treatment method, large investment in coal-water slurry preparation system, Deal with high cost problems, 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 (pH8.1, COD Cr 8200mg / L, volatile phenol 940mg / L, CN - 4.1mg / L, T-N118mg / L), after manganese powder reduction (add 5g of manganese 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 80mg / L, CN - 0.15mg / L, volatile phenol 0.32mg / L, T-N16mg / L.
Embodiment 2
[0008] Embodiment 2: 20m is processed every day 3 Phenol cyanide wastewater (pH8.3, COD Cr 7900mg / L, volatile phenol 830mg / L, CN - 3.6mg / L, T-N105mg / L), after manganese powder reduction (add 10g of manganese powder per liter of wastewater, time 2h, 45℃, 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 74mg / L, CN - 0.10mg / L, volatile phenol 0.23mg / L, T-N 14mg / L.
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