Method for removing iron by oxidation and neutralization in cobalt wet smelting process
A hydrometallurgy and process technology, applied in the field of oxidation and iron removal, can solve the problems of high investment or production costs, low economic benefits, etc., and achieve the effects of high iron removal efficiency, convenient comprehensive recovery, and high iron content
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Embodiment 1
[0016] 1) One-stage acid leaching process: take 300g of copper-cobalt concentrate mineral material and place it in a container, its main chemical components are: Co% 4.44, Cu% 13.39, Fe% 3.18, Mn% 0.32, and then slowly add 51ml of industrial sulfuric acid, And control the solid-liquid ratio to be 1:10, react at a temperature of 50°C and Ph 1.5-1.0 for 3 hours, and obtain 167.2g of one-stage leaching residue after filtration, the main content of which is: Co% 8.76, Cu% 1.32, Fe %6.78, the obtained one-stage leaching solution enters the copper extraction process.
[0017] 2) Two-stage reducing acid leaching process: Take 100g of one-stage leaching residue, control the solid-liquid ratio to 1:4, add 10ml of industrial sulfuric acid and 13.14g of reducing agent sodium metabisulfite, and react at a temperature of 80°C and Ph 0.5-1.0 for 2.5 Hours, the 400ml secondary leachate obtained after filtration contains total Fe5.3g / l, Fe 2+ 5.12g / l; 81.92g of second-stage leaching residue,...
Embodiment 2
[0021] 1) One-stage acid leaching process: take 300g of copper-cobalt concentrate mineral material and place it in a container, its main chemical components are: Co% 4.44, Cu% 13.39, Fe% 3.18, Mn% 0.32, and then slowly add 51ml of industrial sulfuric acid, And control the solid-liquid ratio to be 1:10, react at a temperature of 50°C and Ph 1.5-1.0 for 3 hours, and obtain 167.2g of one-stage leaching residue after filtration, the main content of which is: Co% 8.76, Cu% 1.32, Fe %6.78, the obtained one-stage leaching solution enters the copper extraction process. This process was repeated once more, and one stage of leaching residue was accumulated to 334.4g.
[0022] 2) Two-stage reducing acid leaching process: Take 100g of one-stage leaching residue, control the solid-liquid ratio to 1:4, add 10ml of industrial sulfuric acid and 13.14g of reducing agent sodium metabisulfite, and react at a temperature of 80°C and Ph 0.5-1.0 for 2.5 Hours, the 400ml secondary leachate obtained...
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