Treatment method of wastewater produced from C-D total solvent production
A technology for total solvent and waste water, which is applied in the field of treatment of waste water from the production of total solvent of acetonitrile, can solve the problems of high concentration and it is difficult to discharge the waste water stably up to the standard, and achieves the effects of avoiding pollution, obvious economic and environmental benefits, and improving efficiency.
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Embodiment 1
[0007] Embodiment 1: Treat 1m every day 3 Bingding total solvent wastewater (component: COD Cr 39000 mg / L, T-N40.8 mg / L, SS29000mg / L T-P4.2mg / L, chroma 720), after liquid-solid separation, iron-aluminum-zinc composite powder reduction (1h, 40℃, CO 2 Pressure 0.6MPa, adding iron-aluminum-zinc composite powder 15g per liter of wastewater), anaerobic (pH8.5, 72h, 25°C-35°C), aerobic (4h) and biological filter tower (total thickness of porous ceramsite packing layer 1m , hydraulic load 50m 3 / m 2 .d) COD of effluent after treatment Cr It is 44mg / L, T-N5.3mg / L, T-P0.2mg / L, chromaticity 10.
Embodiment 2
[0008] Embodiment 2: Treat 5m every day 3 Bingding total solvent wastewater (component: COD Cr 41000 mg / L, T-N38.5mg / L, SS31500mg / L, T-P4.7mg / L, chroma 760), after liquid-solid separation, iron-aluminum-zinc composite powder reduction (2.5h, 25℃, CO 2 Pressure 0.1MPa, adding 5g of iron-aluminum-zinc composite powder per liter of wastewater), anaerobic (pH7.0, 24h, 35℃~55℃), aerobic (6h) and biological filter tower (total thickness of activated carbon packing layer 2m, hydraulic Load 150m 3 / m 2 .d) COD of effluent after treatment Cr It is 46mg / L, T-N5.0mg / L, T-P0.2mg / L, chromaticity 12.
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