Method for selectively extracting cobalt and nickel from nickel sulfide concentrate
A technology of nickel sulfide refining and nickel sulfide, which is applied in the field of selective extraction of cobalt and nickel, can solve problems affecting recycling, achieve the effects of reducing pollution, realizing selective and efficient leaching at atmospheric pressure, and improving resource utilization
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Embodiment 1
[0116] Embodiment 1: the preparation of nickel sulfide concentrate leachate
[0117] Step 1: mixing the nickel sulfide concentrate with water to form a nickel sulfide concentrate slurry with a concentration of 25%, and ball milling the nickel sulfide concentrate slurry to form an ultra-fine ground nickel sulfide concentrate.
[0118] Step 2, placing the ultra-finely ground nickel sulfide concentrate in a reaction furnace and adding sulfuric acid solution as a leaching solution, and feeding oxygen at a predetermined pressure into the leaching solution to leach the ultrafinely ground nickel sulfide Metal elements in the concentrate to obtain a nickel sulfide concentrate leaching solution, the metal elements at least include copper, iron, cobalt, nickel, magnesium and calcium elements.
[0119] (1) Investigate the effect of fine grinding particle size on the preparation of nickel sulfide concentrate leaching solution
[0120] Wherein, the condition of selective reaction is: the ...
Embodiment 2
[0147] Embodiment 2: Removal of iron ions in nickel sulfide concentrate leachate
[0148] Step 1. Place the nickel sulfide concentrate leachate obtained under the optimized process conditions of Example 1 in a reactor and heat it to 60° C. with a constant temperature water bath and adjust the pH value of the leachate to 1.2, and then pour the leachate into the leachate An oxidizing agent is added to oxidize ferrous ions in the leaching solution to ferric ions to form a first solution.
[0149] Step 2. Use potassium ferricyanide to detect whether there are ferrous ions remaining in the first solution. If there are no ferrous ions, raise the temperature of the first solution to 90° C., and then add sodium carbonate The solution adjusts the pH value of the first solution to 1.8 to carry out a precipitation reaction, so that the iron ions in the first solution react to form a precipitate. After the reaction is completed, adjust the first solution to a predetermined end point pH va...
Embodiment 3
[0167] Embodiment 3: remove calcium ion and magnesium ion in nickel sulfide concentrate leachate
[0168] The second solution obtained under the optimized process conditions of Example 2, that is, the leaching solution from which iron ions have been removed, is placed in a constant temperature water bath and stirred, and sodium carbonate solution is added to make the second solution reach a predetermined pH value, and the Add sodium fluoride in the second solution as a precipitating agent, the magnesium ions and calcium ions in the second solution react with sodium fluoride, and after the reaction is completed, solid-liquid separation is carried out to obtain the third solution of the liquid phase, that is, to remove The leaching solution of calcium and magnesium ions was removed.
[0169] (1) Investigate the effect of the end point pH value on the removal of calcium ions and magnesium ions in the nickel sulfide concentrate leachate.
[0170] Wherein, the selected reaction co...
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