Method for preparing manganese sulfate solution by using sulphur dioxide gas leach manganese dioxide ore

Abstract

The invention discloses a method for preparing a manganese sulphate solution by leaching pyrolusite with sulfur dioxide gas. The method mainly comprises: pyrolusite and water are prepared into pyrolusite slurry with a liquid to solid ratio of between 5:1 and 1:1; the slurry, the sulfur dioxide gas and oxygen are continuously passed into a reactor provided with two stages of absorbing and leaching reaction chambers which are arranged and connected serially up and down; and absorbing and leaching reactions are carried out in the two absorbing and leaching reaction chambers sequentially at normal temperature, wherein each stage of absorbing and leaching reaction chamber is provided with a stirrer of no less than 5 kW for each cubic meter, the mass flow of the slurry is determined by the stoichiometric ratio of manganese dioxide required by the mass flow of the sulfur dioxide, and the amount of the added oxygen is determined by the pH values of reaction systems in the absorbing and leaching reaction chambers. Another invention applied by the applicant of the invention discloses a reactor for use in pyrolusite leaching. The reactor realizes stable and continuous production, achieves high sulfur and manganese resources recovery rate, meets tail gas exhaust standards and can effectively suppress the generation of MnS2O6 at the same time.

Description

technical field [0001] The invention relates to pyrolusite leaching technology, more specifically, relates to a method for performing absorption and leaching reaction with sulfur dioxide and pyrolusite, so that sulfur resources and manganese resources can be comprehensively and complementary utilized. Background technique [0002] At present, the main methods of hydrometallurgical leaching of pyrolusite are: (1) ferrous sulfate method, the mixed solution of manganese sulfate and ferric sulfate is generated by the reaction of pyrolusite and ferrous sulfate, and then manganese sulfate solution is obtained through purification and iron removal (2) two mines add acid method, adopt pyrolusite and pyrite to react under the condition that sulfuric acid exists to generate the mixed solution of manganese sulfate and ferric sulfate, and mixed solution makes manganese sulfate solution through purification and iron removal. Due to the high content of iron impurities brought in by the mi...

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Problems solved by technology

[0006] (1) Although the process can realize the continuity of production, it needs to switch between the main and secondary reaction pools instead of series reactors in terms of its operation steps. Therefore, it is still a batch reaction operation in essence, and the management is complicated;

[0007] (2) Aeration type mixers or pumps equipped with suction pipes are generally used for oxygenation and aeration in the field of sewage biochemical treatment. The basic principle of gas dispersion is to disperse the gas into the liquid by the shear impact of the liquid, so The operation of this type of equipment generally requires the gas-water volume ratio to reach 5-10 (L / L). If the gas-water ratio is too high, the sulfur dioxide gas will not be able to disperse, which will affect the absorption rate of sulfur dioxide;

[0008] (3) The volume flow of sulfur dioxide gas per unit time that needs to be pumped in industrial production is very large, often as high as thousands to tens of thousands of m 3 / h, while aeration mixers or pumps with suction pipes are mainly used in industrial occasions with less volume flow per unit time, generally hundreds of m 3 / h, so it is difficult to apply to large-scale industrial production such as sulfur dioxide leaching pyrolusite, which limits the actual industrial application of this method.

The reason is mainly due to the following two key common problems in the leaching process that have not been resolved: (1) The equipment used cannot realize continuous reaction operation. Under the condition of intermittent reaction, the pulp is added at one time. Metering ratio, the absorption and utilization rate of sulfur dioxide gas is inversely proportional to the leaching rate of manganese. As the reaction progresses, the leaching rate of manganese is getting higher and higher, while the absorption and utilization rate of sulfur dioxide gas is getting lower and lower, which leads to the discharged The emission of sulfur dioxide gas exceeds the standard seriously, which not only wastes sulfur resources, but also causes serious environmental pollution problems at the same time; (2) using SO 2 The essence of solution leaching pyrolusite and pyrolusite pulp flue gas desulfurization process is SO 2 with MnO 2 complex reaction between the generated MnSO 4 often accompanied by MnS 2 o 6 , if the solution is directly used to produce manganese sulfate, most of the MnS 2 o 6 Will decompose into MnSO when heated 4 and SO 2 , if MnS 2 o 6 Excessive content will still affect the MnSO 4 ·H 2 O quality, measures are needed to suppress MnS 2 o 6 generation

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