Preparation method of manganese sulfate for electrolytic manganese dioxide
A technology of electrolytic manganese dioxide and manganese sulfate, applied in the direction of electrolysis components, electrolysis process, process efficiency improvement, etc., can solve the problems of poor impurity removal effect, low manganese sulfate rate, high impurity removal cost, etc., to reduce processing pressure, Strong adsorption capacity, the effect of reducing production costs
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Embodiment 1
[0018] a. Manganese sulfate leaching and neutralization and iron removal: Put manganese oxide powder, pyrite powder, and industrial sulfuric acid with a particle size of ≥150 mesh into the leaching reaction tank at a weight ratio of 10000g: 1200g: 1800g, and feed sulfur dioxide at the same time SO 2 Gas, manganese oxide ore powder and sulfur dioxide SO 2 The ratio of the amount of gas introduced is 10000g: 2.5mol, reacted for 4.0 hours at a temperature of 105°C and a pressure of 115Kpa, and the crude manganese sulfate slurry is obtained by leaching; Iron ions in crude manganese sulfate solution, so that the concentration of iron Fe≤10 -5 mol / L. The content of Mn in the manganese oxide ore powder used in the present invention is 25%, the content of S in the pyrite powder is 25%, and the industrial sulfuric acid is more than or equal to 97%.
[0019] b. Sulfide precipitation and impurity removal: heating iron Fe concentration ≤ 10 -5 mol / L crude manganese sulfate solution to...
Embodiment 2
[0024] a. Manganese sulfate leaching and neutralization and iron removal: put manganese oxide ore powder, pyrite powder and industrial sulfuric acid with a particle size of ≥150 mesh into the leaching reaction tank at a weight ratio of 10000g: 1500g: 1500g, and feed sulfur dioxide at the same time SO 2 Gas, manganese oxide ore powder and sulfur dioxide SO 2 The ratio of the gas feed rate is 10kg: 2.5mol, react for 4.0 hours at a temperature of 110°C and a pressure of 120Kpa, and obtain crude manganese sulfate slurry; neutralize and remove manganese oxide ore powder with calcium carbonate Iron ions in crude manganese sulfate solution, so that the concentration of iron Fe≤10 -5 mol / L. The content of Mn in the manganese oxide powder used in the present invention is 15%, the content of S in the pyrite powder is 20%, and the industrial sulfuric acid is more than or equal to 97%.
[0025] b. Sulfide precipitation and impurity removal: heating iron Fe concentration ≤ 10 -5 mol / L ...
Embodiment 3
[0030] a. Manganese sulfate leaching and neutralization and iron removal: Put manganese oxide powder, pyrite powder, and industrial sulfuric acid into the leaching reaction tank with a weight ratio of 10000g: 800g: 2200g, and feed sulfur dioxide at the same time SO 2 Gas, manganese oxide ore powder and sulfur dioxide SO 2 The ratio of the gas feed rate is 10000g: 4.0mol, reacted for 2.0 hours at a temperature of 100°C and a pressure of 105Kpa, and obtained crude manganese sulfate slurry; neutralized with calcium carbonate to remove manganese oxide ore powder acid leached Iron ions in crude manganese sulfate solution, so that the concentration of iron Fe≤10 -5 mol / L. The content of Mn in the manganese oxide ore powder used in the present invention is 20%, the content of S in the pyrite powder is 35%, and the industrial sulfuric acid is more than or equal to 97%.
[0031] b. Sulfide precipitation and impurity removal: heating iron Fe concentration ≤ 10 -5 mol / L crude mangane...
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