Synchronized production method of reducing leaching and oxidizing deironing of cobalt-copper ore
A technology for oxidative iron removal and production method, applied in the field of chemical industry, can solve the problems of high cost, large consumption, time consumption, etc., and achieve the effects of reducing direct production cost, improving production efficiency, and improving metal recovery rate
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Embodiment 1
[0014] A production method of cobalt-copper ore reduction, leaching, oxidation, and iron removal, including the following steps:
[0015] The cobalt-copper ore is crushed and slurried into cobalt-copper slurry. The cobalt-copper slurry is leached with sulfuric acid with a molar concentration of 1.6mol / l. The volume ratio of cobalt-copper slurry to sulfuric acid is 20:1, and the temperature is controlled at 75°C, while stirring, add 4% of the total amount of cobalt-copper ore sodium sulfite for reductive leaching, control the mass percentage of cobalt in the wet slag to 0.13%, and the mass percentage of copper to 0.2%. Iron, control the reaction temperature at 90℃, the reaction time is 1 hour, slowly add calcium carbonate to adjust the pH value of the solution to 2.0, and at the same time according to the Fe in the solution 2+ Slowly add cobalt-copper slurry to remove iron by oxidation. The cobalt-copper slurry is added at 50kg, the dry ore ratio is 1g / L iron, and the electrode pot...
Embodiment 2
[0017] A production method of cobalt-copper ore reduction, leaching, oxidation, and iron removal, including the following steps:
[0018] The cobalt-copper ore is crushed and slurried into a cobalt-copper slurry. The cobalt-copper slurry is leached with sulfuric acid with a molar concentration of 1.6mol / l. The volume ratio of the cobalt-copper slurry and sulfuric acid is 50:3, and the temperature is controlled at 80℃, under the condition of stirring, add 5% of the total amount of cobalt copper ore sodium metabisulfite for reductive leaching, control the mass percentage of cobalt in the wet slag to 0.17%, and the percentage of copper to 0.22%, while directly heating up In addition to iron, control the reaction temperature at 92℃, the reaction time is 2.5 hours, slowly add sodium carbonate to adjust the pH value of the solution to 2.8, and at the same time according to the Fe in the solution 2+ Slowly add cobalt-copper slurry to remove iron by oxidation. The cobalt-copper slurry is ...
Embodiment 3
[0020] A production method of cobalt-copper ore reduction, leaching, oxidation, and iron removal, including the following steps:
[0021] The cobalt-copper ore is crushed and slurried into a cobalt-copper slurry. The cobalt-copper slurry is leached with sulfuric acid with a molar concentration of 1.6 mol / l. The volume ratio of the cobalt-copper slurry to sulfuric acid is 100:7, and the temperature is controlled at At 85°C, while stirring, add 6% of the total amount of cobalt-copper ore sulfur dioxide for reduction leaching, control the mass percentage of cobalt in the wet slag to 0.18%, and the mass percentage of copper to 0.25%, and directly increase the temperature to remove Iron, control the reaction temperature to 95℃, the reaction time is 4 hours, slowly add sodium hydroxide to adjust the pH value of the solution to 3.5, and at the same time according to the Fe in the solution 2+ Slowly add cobalt-copper slurry to remove iron by oxidation. The cobalt-copper slurry is added in...
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