Synchronized production method of reducing leaching and oxidizing deironing of cobalt-copper ore
A technology of oxidation iron removal and production method, which is applied in the chemical industry, can solve the problems of high cost, large consumption, and time consumption, and achieve the effects of reducing direct production costs, improving production efficiency, and increasing metal recovery rate
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Embodiment 1
[0014] A production method for simultaneous reduction, leaching, oxidation and iron removal of cobalt-copper ore, comprising the following steps:
[0015] The cobalt-copper ore is crushed and adjusted to form a cobalt-copper slurry, and sulfuric acid with a molar concentration of 1.6mol / l is added to the cobalt-copper slurry for leaching. The volume ratio of the cobalt-copper slurry to sulfuric acid is 20:1, and the temperature is controlled at 75°C, under the condition of stirring, add 4% sodium sulfite of the total amount of cobalt-copper ore for reduction leaching, control the mass percentage of cobalt in the wet residue to 0.13%, and the mass percentage of copper to 0.2%, and directly increase the temperature to remove Iron, control the reaction temperature at 90°C, 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+ content, slowly add cobalt-copper slurry to ...
Embodiment 2
[0017] A production method for simultaneous reduction, leaching, oxidation and iron removal of cobalt-copper ore, comprising the following steps:
[0018] The cobalt-copper ore is crushed and slurried to form a cobalt-copper slurry. Sulfuric acid with a molar concentration of 1.6mol / l is added to the cobalt-copper slurry for leaching. The volume ratio of the cobalt-copper slurry to sulfuric acid is 50:3, and the temperature is controlled at 80°C, with stirring, add 5% sodium pyrosulfite of the total amount of cobalt-copper ore for reduction leaching, control the mass percentage of cobalt in the wet residue to 0.17%, and the mass percentage of copper to 0.22%, and directly increase the temperature In addition to iron, control the reaction temperature at 92°C, 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 oxidize and remove i...
Embodiment 3
[0020] A production method for simultaneous reduction, leaching, oxidation and iron removal of cobalt-copper ore, comprising the following steps:
[0021] The cobalt-copper ore is crushed and adjusted to form a cobalt-copper slurry. Sulfuric acid with a molar concentration of 1.6mol / l is added to the cobalt-copper slurry for leaching. The volume ratio of the cobalt-copper slurry to sulfuric acid is 100:7, and the temperature is controlled at 85°C, under the condition of stirring, adding 6% sulfur dioxide of the total amount of cobalt-copper ore for reduction leaching, controlling the mass percentage of cobalt in the wet slag to 0.18%, and the mass percentage of copper to 0.25%. Iron, control the reaction temperature at 95°C, 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 oxidize and remove iron. The amount of cobalt-copper slu...
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