Preparation method of specia electrolytic manganese dioxide for button type alkaline zinc/manganese dioxide cell
A technology of electrolytic manganese dioxide and manganese dioxide, applied in the direction of manganese oxide/manganese hydroxide, battery electrodes, electrolytic components, etc., can solve the problems of low efficiency, long preparation process time, complex and cumbersome preparation process, etc., and achieve particle size distribution Highly uniform, highly uniform quality, and reasonable crystal phase structure
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Embodiment 1
[0024] a. Manganese sulfate leaching: 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: 1000g: 2000g. The stirring speed is 60rpm and the temperature is 90 °C for 2 hours, then adjust the stirring speed to 30rpm, the temperature is 95 °C, and simultaneously feed sulfur dioxide SO 2 Gas, manganese oxide ore powder and sulfur dioxide SO 2 The ratio of gas feeding rate is 10000g:2.0mol, the reaction time is 1.5 hours, and the crude manganese sulfate solution is obtained by leaching. The manganese content in the manganese oxide ore powder used in the present invention is 20%, the S in the pyrite powder is more than 20%, and the concentrated sulfuric acid is industrial grade H 2 SO 4 ≥97%.
[0025] b. Neutralization and iron removal: under normal temperature conditions, add ammonium bicarbonate to the crude manganese sulfate solution slurry obtained in step a ...
Embodiment 2
[0031] a. Manganese sulfate leaching: 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: 1200g: 1800g. °C for 2 hours, then adjust the stirring speed to 50rpm and the temperature to 90 °C, while feeding sulfur dioxide SO 2 Gas, manganese oxide ore powder and sulfur dioxide SO 2 The ratio of gas feeding rate is 10000g:0.5mol, the reaction time is 1.0 hour, and the crude manganese sulfate solution is obtained by leaching. The manganese content in the manganese oxide ore powder used in the present invention is 16%, the S in the pyrite powder is ≥ 20%, and the concentrated sulfuric acid is industrial grade H 2 SO 4 ≥97%.
[0032] b. Neutralization and iron removal: the operation steps are the same as in Example 1.
[0033] c. Heavy metal impurity removal: heat the crude manganese sulfate solution obtained in step b to 85-90°C, slowly add barium sulfide at a r...
Embodiment 3
[0038] a. Manganese sulfate leaching: 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: 1200g: 1000g. Stirring speed is 80rpm, temperature is 87 °C for 2.5 hours, then adjust the stirring speed to 40rpm and the temperature to 93 °C, while feeding sulfur dioxide SO 2 Gas, manganese oxide ore powder and sulfur dioxide SO 2 The ratio of gas feeding rate is 10000g:3.0mol, the reaction time is 1.5 hours, and the crude manganese sulfate solution is obtained by leaching. The manganese content in the manganese oxide ore powder used in the present invention is 18%, the S in the pyrite powder is more than or equal to 20%, and the concentrated sulfuric acid is industrial grade H 2 SO 4 ≥97%.
[0039] b. Neutralization and iron removal: the operation steps are the same as in Example 1.
[0040] c. Heavy metal impurity removal: heat the crude manganese sulfate soluti...
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