利用双氧水为还原剂湿法浸出电解锰阳极泥中锰的研究

Hydrometallurgy leaching of manganese from electrolytic manganese anode slime using hydrogen peroxide as reducing agent

  • 摘要: 电解锰阳极泥是生产电解金属锰时阳极产生的副产物,其中含有大量锰、铅等资源。如何高效浸出电解锰阳极泥中的锰是实现其资源化利用的关键,本研究提出了一种H2SO4−H2O2浸出体系强化电解锰阳极泥中锰浸出的新方法,研究了H2O2和H2SO4用量、反应温度、反应时间以及固液比对电解锰阳极泥中锰浸出率的影响。研究结果表明,在阳极泥与H2O2质量比1∶0.8、阳极泥与H2SO4质量比1∶0.9、反应温度45 ℃、固液质量比1∶10条件下浸出反应15 min,锰的浸出率可达97.23%,浸出渣中Pb的质量分数高达53.71%。浸出机理分析表明,酸性条件下电解锰阳极泥中锰氧化物被H2O2还原浸出,浸出液中Mn主要以MnSO4存在,浸出渣中Pb主要以PbSO4富集。本研究结果为电解锰阳极泥的资源化利用提供了一种新思路。

     

    Abstract: Manganese is one of the important strategic resources in China, and there is a saying that “no manganese, no steel”. In 2020, China’s output of electrolytic metal manganese was 1501300 tons, accounting for 96.5% of the global output. At present, manganese metal is mainly obtained using the electrodeposition process. Electrolytic manganese anode slime (EMAS) is a kind of solid waste generated during the production of electrolytic metal manganese, which contains a significant amount of manganese, lead, and other resources. Every year, 60000−180000 tons of EMAS will be discharged in China, and direct discharge will cause severe environmental pollution. Cleaning and efficiently leaching Mn from EMAS is the key to realizing its resource utilization. A large number of studies have achieved efficient leaching of manganese from EMAS. Still, there are a number of issues, such as complicated processes, high leaching cost, a large amount of reducing agent, and residual organic matter in the leaching solution. Therefore, it is urgent to find a new method for efficient clean leaching of manganese from EMAS. This study proposed a new method of enhancing manganese leaching from EMAS with an H2SO4–H2O2 leaching system. The effects of the dosage of H2SO4 and H2O2, reaction temperature, reaction time, and solid–liquid ratio on the leaching efficiency of manganese from EMAS were studied. The results show that the leaching efficiency of manganese was 97.23%, and the content of Pb in the leaching residue was 53.71%, when the mass ratio of EMAS to H2O2 was 1∶0.8, the mass ratio of EMAS to H2SO4 was 1∶0.9, the leaching temperature was 45 ℃, the solid–liquid mass ratio was 1∶10 and the leaching time was 15 min. Leaching mechanism analysis showed that manganese oxide leaching in EMAS was reduced by H2O2 under acidic conditions, and Mn mainly exists in the leaching solution as MnSO4, as well as Pb in leaching residue is mainly enriched with PbSO4. This study offers a new idea for resource utilization of EMAS.

     

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