Device for treating nickel-cobalt sewage in the hydrometallurgy industry by electrolytic method
A technology of hydrometallurgy and electrolysis, which is applied in the field of equipment for electrolytic treatment of nickel-cobalt sewage in the hydrometallurgy industry. It can solve the problems of high sewage treatment cost, secondary pollution, and poor effect, and achieve low facility investment and operation costs. , Less labor input and shorter process flow
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Embodiment 1
[0032] Sewage containing Ni52.6mg / L, Co14.3mg / L, PH3.85, COD426.4mg / L, P organic 5.7mg / L, oil 21.7mg / L in 0.06m 3 The flow rate of / min is pumped into the electrolytic cell, the cell voltage is set to 2.9V, and the current density is adjusted to 108.52A / m 2 , electrolyzed for 30min, the liquid after electrolysis was filtered and tested, Ni: 0.25mg / L, Co: 0.20mg / L, PH7.37, COD106.5mg / L, P organic 1.9mg / L, oil in water 7.3 mg / L.
Embodiment 2
[0034] Sewage containing Ni90.4mg / L, Co19.5mg / L, PH3.62, COD956.4mg / L, P organic 11.9mg / L, oil 43.3mg / L in 0.08m 3 The flow rate of / min is pumped into the electrolytic cell, the cell voltage is set to 2.6V, and the current density is adjusted to 60.34A / m 2 , electrolyzed for 35 minutes, after electrolysis, the solution was filtered and detected, Ni: 0.46mg / L, Co: 0.34mg / L, PH6.75, COD195.2mg / L, P organic 2.8mg / L, oil in water 9.4 in the filtrate mg / L.
Embodiment 3
[0036] Pump sewage containing Ni136.2mg / L, Co51.6mg / L, PH3.81, COD673.8mg / L, P organic 8.7mg / L, and oil 29.6mg / L into the electrolytic cell at a flow rate of 0.07m3 / min Inside, set the cell voltage to 3.0V and adjust the current density to 105.16A / m 2 , electrolyzed for 40min, after electrolysis, the solution was filtered and tested, Ni: 0.39mg / L, Co: 0.31mg / L, PH7.29, COD134.6mg / L, P organic 2.3mg / L, oil in water 7.8 in the filtrate mg / L.
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