Method for deeply removing impurities of manganese dioxide electrolyte
A manganese dioxide and electrolyte technology, applied in the direction of non-aqueous electrolyte batteries, electrolytic components, electrolytic process, etc., can solve the problems of high cost of impurity removal and poor effect of impurity removal, so as to reduce production cost, reduce burden, realize The effect of economization
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Embodiment 1
[0018] (1) Neutralization and removal of iron: under normal temperature conditions, add calcium carbonate to the crude manganese sulfate slurry to neutralize the residual H in the solution 2 SO 4 , so that the pH of the solution is 5.0, stop adding calcium carbonate, and detect that the concentration of ferrous ions in the solution is ≤10 -5 mol / L is qualified, if the concentration of ferrous ions>10 -5 mol / L, add adsorbent until the content of ferrous ions in the mixed solution is qualified, continue to add calcium carbonate to adjust the pH value to 6.0 after the ferrous ions are qualified, and detect the concentration of ferric ions in the mixed solution ≤ 10 -5 mol / L is qualified, if the concentration of ferric ion>10 -5 mol / L, continue to add calcium carbonate until the ferric ion content in the mixed solution is qualified, filter and remove the filter residue to obtain crude manganese sulfate solution.
[0019] (2) Sulfide precipitation and impurity removal: heat the ...
Embodiment 2
[0024] (1) Neutralization and iron removal: with embodiment 1.
[0025] (2) Sulphide precipitation and impurity removal: heat the crude manganese sulfate solution obtained in step (1) to 85° C., slowly add barium sulfide BaS and sodium sulfide Na 2 Sulfur mixture of S, 30% sodium sulphide Na 2 S solution and 30% barium sulfide BaS solution are mixed according to the volume ratio of 0.1L:0.9L, the speed of adding the vulcanization mixture is 2g / L / min, and the concentration of Cu, Pb, Ni, Co is detected every 30min, when Cu≤ 2ppm, Pb ≤ 3ppm, Ni ≤ 2ppm, Co ≤ 2ppm, stop adding the vulcanization mixture, and filter to obtain the manganese sulfate solution after sulfide precipitation and impurity removal.
[0026] (3) Deep removal of impurities by adsorbent: Add electrolytic waste liquid to the manganese sulfate solution obtained in step (2) to adjust the pH of the reaction solution to 4.5, and add adsorbent to make the concentrations of trace elements As, Sb, and Mo all ≤0.005ppm ...
Embodiment 3
[0030] (1) Neutralization and iron removal: with embodiment 1.
[0031] (2) Sulfide precipitation and impurity removal: heating the crude manganese sulfate solution obtained in step (1) to 88°C, slowly adding barium sulfide BaS and sodium sulfide Na 2 Sulfur mixture of S, 25% sodium sulphide Na 2 S solution and 25% barium sulfide BaS solution are mixed according to the volume ratio of 0.2L:0.8L, the speed of adding the vulcanization mixture is 4g / L / min, and the concentration of Cu, Pb, Ni, Co is detected every 30min, when Cu≤ 2ppm, Pb ≤ 3ppm, Ni ≤ 2ppm, Co ≤ 2ppm, stop adding the vulcanization mixture, and filter to obtain the manganese sulfate solution after sulfide precipitation and impurity removal.
[0032] (3) Deep removal of impurities by adsorbent: Add electrolytic waste liquid to the manganese sulfate solution obtained in step (2) to adjust the pH of the reaction solution to 4.0, and add adsorbent to make the concentrations of trace elements As, Sb, and Mo all ≤0.005p...
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