Production method for simultaneously conducting mixed leaching and iron removal of cobalt concentrate and cobalt intermediate product
A production method and concentrate technology, which is applied in the production field of cobalt concentrate and cobalt intermediate products mixed leaching-iron removal simultaneously, can solve the problems of poor filtration performance, low cobalt liquid main taste, low metal recovery rate, etc., and achieve The effect of saving production cost and improving the content of main taste
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Embodiment 1
[0028] A cobalt concentrate and cobalt intermediate product mixed leaching-iron removal production method, comprising the following steps:
[0029] The cobalt concentrate and cobalt intermediate product are made into cobalt concentrate slurry and cobalt intermediate product slurry respectively after ball milling, and the mass concentration of cobalt concentrate slurry is 1.84 g / cm 3 Sulfuric acid leaching, the volume ratio of cobalt concentrate pulp to sulfuric acid is 10:1, the temperature is controlled at 65°C, under the condition of stirring, excess sodium sulfite is added for reduction leaching, the pH of the control solution is 1.5, when the slurry in the slurry When the slag was off-white, the temperature was raised to 95°C, and after the temperature stabilized, according to the Fe in the solution, 2+ content, add cobalt concentrate slurry as an oxidant to oxidize and remove iron, and the amount of cobalt concentrate slurry (calculated by the amount of cobalt metal) is 1...
Embodiment 2
[0033] A cobalt concentrate and cobalt intermediate product mixed leaching-iron removal production method, comprising the following steps:
[0034] The cobalt concentrate and cobalt intermediate product are made into cobalt concentrate slurry and cobalt intermediate product slurry respectively after ball milling, and the mass concentration of cobalt concentrate slurry is 1.84 g / cm 3 Sulfuric acid leaching, the volume ratio of cobalt concentrate pulp to sulfuric acid is 10:1, the temperature is controlled at 65 ° C, under the condition of stirring, excessive sodium metabisulfite is added for reduction leaching, and the pH of the solution is controlled to be 1.0. When the slag was off-white, the temperature was raised to 95°C at this time, and after the temperature stabilized, according to the Fe in the solution, 2+ content, add cobalt concentrate slurry as an oxidant to oxidize and remove iron, and the amount of cobalt concentrate slurry (calculated by the amount of cobalt meta...
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