Method for selective precipitation separation of nickel and manganese by utilizing CO2 gas
A precipitation separation and CO2 technology, applied in the field of selective precipitation and separation of nickel and manganese, can solve the problems of difficult filtration, incomplete separation, complicated control, etc., and achieve the effect of good filtration performance, elimination of local excess concentration, and complete manganese precipitation
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Embodiment 1
[0022] (1) Get 200ml of nickel-manganese solution, wherein the nickel ion content is 5.9g / l, the manganese ion content is 11g / l, the pH of the solution is 3.7, add ammonium sulfate in the nickel-manganese solution, and the quality of the ammonium salt added is 52.9 g;
[0023] (2) Add 8g of sodium hydroxide to adjust the pH value of the solution to 8.9;
[0024] (3) Maintain the temperature of the solution at 25°C and pass CO 2 Until the pH of the solution is 7.5, the flow rate of the gas is 7.2 l / h, and the time for feeding the gas is 1.7 hours;
[0025] (4) The manganese carbonate precipitate was filtered and washed, and then dried to obtain 4.5 g of filter residue, which was analyzed after drying, and the nickel content was 0.56%, and the manganese content was 36.6%.
[0026] Finally, the precipitation rate of manganese was 98.7%, and the loss rate of nickel was 1.17%.
Embodiment 2
[0028] (1) get nickel-manganese solution 200ml, wherein nickel ion content is 5.9g / l, and manganese ion content is 11g / l, and the pH of solution is 3.7, adds ammonium sulfate in nickel-manganese solution, and the quality in the ammonium salt of adding is 52.9g;
[0029] (2) Add 8g of sodium hydroxide to adjust the pH value of the solution to 8.8;
[0030] (3) Maintain the temperature of the solution at 35°C and pass CO 2 Until the pH of the solution is 8.2, the flow rate of the gas is 8.1 l / h, and the time for feeding the gas is 0.5 hour;
[0031] (4) The manganese carbonate precipitate was filtered and washed, and then dried to obtain 4.6 g of filter residue, which was analyzed after drying, and the nickel content was 0.13%, and the manganese content was 45.0%.
[0032] Finally, the precipitation rate of manganese was 99.8%, and the loss rate of nickel was 0.27%.
Embodiment 3
[0034] (1) get nickel-manganese solution 200ml, wherein nickel ion content is 5.9g / l, and manganese ion content is 11g / l, and the pH of solution is 3.7, adds ammonium sulfate in nickel-manganese solution, and the quality in the ammonium salt of adding is 52.9g;
[0035] (2) Add 8g of sodium hydroxide to adjust the pH value of the solution to 8.8;
[0036] (3) Maintain the temperature of the solution at 40°C and pass CO 2 Until the pH of the solution is 6.9, the flow rate of the gas is 6.5 l / h, and the time for feeding the gas is 3.3 hours;
[0037] (4) The manganese carbonate precipitate was filtered and washed, and then dried to obtain 4.7 g of filter residue, which was analyzed after drying, and the nickel content was 0.54%, and the manganese content was 46.3%.
[0038] Finally, the precipitation rate of manganese was 99.8%, and the loss rate of nickel was 1.13%.
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