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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

Inactive Publication Date: 2014-02-12
GUANGXI GUILIU CHEM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to overcome the problems of low manganese sulfate rate, poor impurity removal effect and high impurity removal cost in the preparation method of the existing electrolytic manganese dioxide electrolyte—manganese sulfate solution. SO 2 Catalysis, introducing Ca(MnO 4 ) 2 , NaMnO 4 MnO in 4 - As an adsorbent, a preparation method of manganese sulfate for electrolytic manganese dioxide is provided

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

The invention belongs to the field of battery material processing, and specifically relates to a preparation method of manganese sulfate for electrolytic manganese dioxide. The preparation method comprises the steps of manganese sulfate leaching and neutralization for iron removal, impurity removal of heavy metals, electrolysis and post-processing; concretely, manganese oxide ore powder, pyrite powder and an industrial sulphuric acid are subjected to high-temperature and high-pressure leaching in the presence of SO2 so as to prepare a coarse manganese sulfate solution, then the coarse manganese sulfate solution is subjected to iron removal by using calcium carbonate and subjected to primary heavy metal removal by using barium sulphide, and an adsorbent is added to secondarily remove trace elements, so that the concentrations of the trace elements such as As, Sb and Mo are all less than or equal to 0.005 ppm, thereby obtaining a manganese sulfate solution with a good quality. The content of impurities such as Fe, Cu, Pb, Ni, Co, K, Na, Ca, Mg, and the like in the manganese sulfate solution prepared by using the method disclosed by the invention is low, wherein the content of Cu is less than or equal to 2.0 ppm, the content of Pb is less than or equal to 3.0 ppm, the content of Ni is less than or equal to 2.0 ppm, and the content of Co is less than or equal to 2.0 ppm.

Description

technical field [0001] The invention belongs to the field of battery material processing, in particular to a preparation method of manganese sulfate for electrolytic manganese dioxide. Background technique [0002] The preparation of high-purity manganese sulfate solution is an essential pre-process for the manufacture of electrolytic manganese dioxide (EMD) for alkaline zinc-manganese batteries. The development of alkaline zinc-manganese dry batteries has put forward higher and higher requirements for EMD. Its chemical purity is one aspect of this. According to earlier information, the chemical impurities of EMD that affect battery performance can be divided into active components (Hg); nearly harmless components (Mg, Na, Mn); slightly harmful components (Cd, Fe); quite harmful components ( Ni, Co, Mo, Cu) and the most harmful components (Sb, As). These components not only refer to the quantity, but also are related to the valence state, the solubility in the electrol...

Claims

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Application Information

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IPC IPC(8): C22B3/44C22B3/22C22B3/08C25B1/21
CPCY02P10/20
Inventor 罗驰飞邱立铭梁乐忠徐星意范汝平
Owner GUANGXI GUILIU CHEM CO LTD
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