Industrial method for selectively recycling copper and nickel from copper-nickel mud
An industrial method and selective technology, applied in the field of non-ferrous metal resource recycling, can solve the problems of complex composition of copper-nickel sludge, high impurity content, high processing cost, etc., to prevent the overflow and leakage of acid mist, simplify the operation process, improve the The effect of recovery
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Embodiment 1
[0026] Example 1: The appearance of the selected copper-nickel mud is blue-green, mud-like, and the water content is 54%. The main metal element content of drying sampling analysis is as follows:
[0027] elementCu Ni Fe MgCr Cd %35.9711.120.960.520.860.03 element Ca Pb Co Bi Mn Zn % / / 0.140.080.090.97
[0028] Proceed as follows:
[0029] Weigh 500g of the above dry copper-nickel mud, add 1.5L of distilled water to slurry, then slowly add 190ml of concentrated sulfuric acid, control the reaction temperature to 80℃, the pH of the solution is 2.0, and the leaching time is 2 hours; the leachate is precision filtered, and the filtrate is added with water Dilute to 4L and enter the cyclone electrolyzer to remove copper, control the electrowinning temperature to 30℃, and the current density to 200-400A / m 2 , The electrolyte flow rate is 400L / h, the electrowinning time is 5-7 hours, and the copper tube is obtained on the cathode starting electrode. The copper content of the copper r...
Embodiment 2
[0031] Weigh 500g of dry nickel mud, add 2L of distilled water to slurry, then slowly add 195ml of concentrated sulfuric acid, control the reaction temperature to 90℃, the pH of the solution is 3.5, and the leaching time for 1 hour; the leaching solution is precision filtered and the filtrate enters the cyclone electrolysis To remove copper from the tank, control the electrowinning temperature to 65°C, and the current density 400-700A / m 2 , The electrolyte flow rate is 600L / h, the electrowinning time is 2-5 hours, and the copper tube is obtained on the cathode starting electrode. The copper-removed liquid contains 0.2g / L of copper; the copper-removed liquid passes through the heat exchanger and uses The industrial water is cooled, and the temperature of the solution is reduced from about 65°C to the industrial water temperature. Secondly, the low temperature brine at -15°C is passed through the heat exchanger to further cool the final copper removal solution after the heat exchan...
Embodiment 3
[0033] Weigh 500g of dry nickel mud, add 2L of distilled water to slurry, then add the crystallization filtrate in Example 2, then add concentrated acid, control the reaction temperature to 60℃, the pH of the solution is 0.5, and the leaching time is 5 hours; Precise filtration, the filtrate enters the cyclone electrolytic cell to remove copper, the electrowinning temperature is controlled to 50℃, and the current density is 500-600A / m 2 , The electrolyte flow rate is 500L / h, the electrowinning time is 4 hours, and the copper tube is obtained on the cathode starter piece. The copper-removed liquid contains 0.3g / L of copper; the copper-removed liquid passes through the heat exchanger and uses industrial water Perform cooling, reduce the temperature of the solution from about 50°C to industrial water temperature, and then pass the low temperature brine at -15°C through the heat exchanger to further cool the final copper removal solution after the heat exchanger is cooled, and then p...
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