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Lab-scale circulation process of electrolytic manganese production with low-grade pyrolusite leaching by SO_2

机译:SO_2浸出低品位软锰矿的电解锰实验室规模循环工艺

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摘要

A lab-scale circulation process of electrolytic manganese production with low-grade pyrolusite leaching by SO_2 was introduced, exploring its feasibility and stability. Material balances of manganese and sulfur in circu lation process were investigated. Results showed that the circulation process was entirely feasible. SO_2 absorption efficiency of 99.66% and Mn extraction rate of 95.5% were obtained when a two-stage continuous countercurrent leaching process was used. The electrolytic manganese, meeting the needs of national indus try grade standards, could be produced using purified leaching solution. 32 days' continuous running test proved good stability of the circulation process with the current efficiency of 78.1%, electricity consumption of 5396 kW h/t and total Mn recovery rate of 81.77%. The circulation process realized that the electrolytic manganese production with low-grade pyrolusite, has a wide prospect in industrial applications due to the advantages of stable performance, high efficiency and low consumption.
机译:介绍了实验室规模的SO_2低品位软锰矿浸出生产电解锰的循环工艺,探讨了其可行性和稳定性。研究了循环过程中锰和硫的物质平衡。结果表明,循环过程是完全可行的。采用两阶段连续逆流浸出工艺,SO_2的吸收效率为99.66%,Mn的提取率为95.5%。电解锰可以满足国家工业等级标准的要求,可以使用提纯的浸出液生产。连续运行32天的试验证明循环过程具有良好的稳定性,电流效率为78.1%,电耗为5396 kW h / t,总锰回收率为81.77%。循环过程表明,低品位软锰矿电解锰生产具有性能稳定,效率高,消耗低等优点,在工业应用中具有广阔的前景。

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