A method for preparing high-purity copper solution and high-purity cobalt solution by high-pressure leaching of cobalt-iron alloy
A cobalt-iron alloy and high-pressure leaching technology, applied in the field of metallurgy, can solve problems such as the difficulty of utilizing cobalt-iron alloy, and achieve the effects of increasing processes and costs, avoiding processes and costs, and increasing the concentration of cobalt ions
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Embodiment 1
[0028] Step 1. One-stage leaching: Slurry the cobalt-iron alloy with water, add sulfuric acid with a concentration of 98% to carry out atmospheric acid pre-soaking, the amount of inorganic acid is 1.0 times the theoretical amount, the volume-to-mass ratio of liquid to solid is 5:1, and the pre-soaking temperature 40℃, the pre-soaking time is 5h, the slurry after pre-soaking is passed through oxygen, and the oxidative acid leaching is carried out under the condition of the oxygen pressure of 0.8MP. Afterwards, solid-liquid separation is carried out to obtain a section of leachate;
[0029] Step 2, second-stage iron removal: add an appropriate amount of lye to the first-stage leaching solution to adjust the pH value of the solution to 1.0, introduce oxygen, and remove iron under the condition of oxygen pressure of 0.8MP. The iron removal temperature is 120°C. The iron time is 8h, and the solid-liquid separation is carried out after the reaction is completed, and the iron-removed...
Embodiment 2
[0038] Step 1, one-stage leaching: Slurry the cobalt-iron alloy with water, add sulfuric acid with a concentration of 90% to carry out atmospheric acid pre-soaking, the amount of inorganic acid is 1.2 times the theoretical amount, the volume-to-mass ratio of liquid to solid is 6:1, and the pre-soaking temperature at 90°C, the pre-soaking time is 1h, the slurry after pre-soaking is passed through oxygen, and the oxidative acid leaching is carried out under the condition of oxygen pressure of 1.3MP. The temperature of oxidative acid leaching is 120°C, and the leaching time is 8h. Carry out solid-liquid separation to obtain a section of leachate;
[0039] Step 2, second-stage iron removal: add an appropriate amount of lye to the first-stage leaching solution to adjust the pH value of the solution to 1.8, introduce oxygen, and remove iron under the condition of oxygen pressure of 1.3MP. The iron removal temperature is 240°C. The iron time is 1.5h. After the reaction is completed, ...
Embodiment 3
[0048] Step 1, one-stage leaching: Slurry the cobalt-iron alloy with water, add sulfuric acid with a concentration of 90% to carry out atmospheric acid pre-soaking, the amount of inorganic acid is 1.1 times the theoretical amount, the volume-to-mass ratio of liquid to solid is 6:1, and the pre-soaking temperature 70°C, the pre-soaking time is 3h, the pre-soaked slurry is passed through oxygen, and the oxidative acid leaching is carried out under the condition of the oxygen pressure of 1.1MP. The temperature of the oxidative acid leaching is 170°C, and the leaching time is 4h. Carry out solid-liquid separation to obtain a section of leachate;
[0049] Step 2, second-stage iron removal: add an appropriate amount of lye to the first-stage leaching solution to adjust the pH value of the solution to 1.5, introduce oxygen, and remove iron under the condition of oxygen pressure of 1.1MP. The iron removal temperature is 180°C. The iron time is 4.5h, and the solid-liquid separation is ...
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