Preparation method of special electrolytic manganese dioxide for automobile power battery
A technology for electrolysis of manganese dioxide and automobile power batteries, which is applied in the directions of electrolysis components, electrolysis process, and process efficiency improvement, etc., can solve the problems of complicated and tedious preparation process, long preparation process time, poor method specificity, etc., so as to speed up the reaction. , Improve the efficiency of production process and reduce the effect of processing pressure
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Embodiment 1
[0028] 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 80rpm and the temperature is 85 °C for 1.5 hours, then adjust the stirring speed to 60rpm, the temperature is 85 °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:0.5mol, the reaction time is 1.0 hour, and the crude manganese sulfate solution is obtained by leaching. The manganese content of manganese oxide ore powder is 17%, and the effective sulfur content (weight ratio) in pyrite is 25%.
[0029] b, neutralization and removal of iron: under normal temperature conditions, add ammonium bicarbonate to the crude manganese sulfate solution slurry obtained in step a, and neutralize the residual H in the solution 2 SO 4 , so that the pH of the s...
Embodiment 2
[0035] a. Manganese sulfate leaching: put manganese oxide ore powder, pyrite powder, and industrial sulfuric acid with a particle size ≥ 150 meshes into the leaching reaction tank at a weight ratio of 10000g: 800g: 2200g. °C for 2 hours, then adjust the stirring speed to 70rpm 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:2.0mol, the reaction time is 1.2 hours, and the crude manganese sulfate solution is obtained by leaching. The manganese content of manganese oxide ore powder is 15.5%, and the effective sulfur content (weight ratio) in pyrite is 28%.
[0036] b, neutralization and iron removal: with the operation in embodiment 1.
[0037] c. Heavy metal impurity removal: the temperature of the crude manganese sulfate solution obtained in heating step b is raised to 90°C, and barium sulfide BaS and sodium sulfide Na are slowly added 2 The vulcanized mixture of S...
Embodiment 3
[0042] a. Manganese sulfate leaching: Put manganese oxide ore powder, pyrite powder, and industrial sulfuric acid with a particle size ≥150 mesh into the leaching reaction tank at a weight ratio of 10000g: 1200g: 1800g. The stirring speed is 120rpm and the temperature is 85 °C for 1.5 hours, then adjust the stirring speed to 70rpm, 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:1.5mol, the reaction time is 1.5 hours, and the crude manganese sulfate solution is obtained by leaching. The manganese content of manganese oxide ore powder is 16.0%, and the effective sulfur content (weight ratio) in pyrite is more than 30%.
[0043] b, neutralization and iron removal: the same as the operating requirements in Example 1.
[0044] c. Heavy metal impurity removal: the temperature of the crude manganese sulfate solution obtained in heating step b is raised to 90°C, and...
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Abstract
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