硫酸镁废水回用稀土矿浸取工艺试验研究
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甘肃稀土新材料股份有限公司, 甘肃 白银 730922

作者简介:

李向东(1987—),男,甘肃白银人,硕士研究生,高级工程师,主要从事稀土湿法冶炼分离工作。

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甘肃省重大科技专项“基于镁盐循环的高品质稀土化合物材料制备技术研发及产业化”(22ZD6GD061)


Magnesium sulfate wastewater leaching rare earth ore process
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Gansu Rare Earth New Material Limited-Liability Company, Baiyin 730922 , China

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    摘要:

    “三代酸法”稀土分离工艺用到大量镁离子,产生大量的转型硫酸镁废水,废水中含有SO2-4、饱和硫酸钙、Mg2+、油和悬浮物等成分,且水质不稳定,处理难度较大。传统石灰中和法、传统蒸发浓缩法等存在处理成本高、效率低等问题,导致稀土硫酸镁废水的处理一直处于空白状态。本文提出“氢氧化钙中和-回用稀土浸取”的绿色工艺路线,并从硫酸镁废水中和除杂、中和液浸取硫酸稀土过程稀土收率和尾渣含水率等三个方面展开研究,得到以下主要结论。氢氧化钙中和硫酸镁废水沉淀镁的过程主要受溶液pH值的影响,当废水pH=9.5时,SO2-4含量为80.5g/L,Mg2+含量降低至14.7g/L,且氢氧化钙的加入量最小;中和液pH值对浸出尾渣含水率影响较大,pH值较大时,含水率低,滤饼成型度好,当pH=9.5时,稀土浸出率无明显降低,稀土尾渣含水率达到42.3%(生产要求含水率<43.0%),达到进入尾矿库的标准;该工艺采用常规搅拌,原因是硫酸根浓度大于85.0g/L时,高剪切搅拌作用破坏了Ce4+与SO2-4和Mg2+形成的可溶性络合物,使得四价铈与硫酸镁废水形成絮状物析出,堵塞滤饼水流通道,影响固液分离。采用本文方法中和硫酸镁废水后再回用到稀土焙砂浸取工艺,稀土浸出不受影响,可以实现硫酸镁废水的循环利用。

    Abstract:

    The third generation sulfuric acid rare earth separation process uses a lot of magnesium ions, which produces a lot of transformed magnesium sulfate wastewater. The wastewater contains SO2-4, saturated calcium sulfate, Mg2+, oil and suspended solids, and the water quality is unstable, so it is difficult to treat. Traditional lime neutralization method and traditional evaporation concentration method have some problems, such as high treatment cost and low efficiency, which lead to the treatment of rare earth magnesium sulfate wastewater has been in a blank state. This paper proposes a green process route of “calcium hydroxide neutralization-reuse of rare earth leaching”, and conducts research from three aspects: neutralization and impurity removal of magnesium sulfate wastewater, rare earth recovery rate in the neutralization liquid leaching process of sulfate rare earth, and moisture content of tailings. The following main conclusions are obtained. The process of neutralizing magnesium sulfate wastewater by calcium hydroxide is mainly affected by the pH value of the solution, when the wastewater pH is 9.5, the content of SO2-4 is 80.5g/L, the content of Mg2+ decreases to 14.7g/L, and the addition of calcium hydroxide is the smallest. The pH value of neutralization solution has a great influence on the water content of leaching tailings. When the pH value is large, the water content is low and the cake forming degree is good, when pH=9.5, the leaching rate of rare earth did not decrease obviously, and the water content of rare earth tailings reached 42.3% (the water content required for production was less than 43.0%), which reached the standard of entering the tailings pond. Conventional stirring is adopted in this process, because when the concentration of sulfate radical is more than 85.0g/L, the soluble complex formed by Ce4+, SO2-4 and Mg2+ is destroyed by high-shear stirring, so that tetravalent cerium and magnesium sulfate wastewater form flocs to precipitate, blocking the water flow channel of filter cake and affecting solid-liquid separation.Using this method to neutralize magnesium sulfate wastewater and then reuse it in rare earth calcine leaching process, rare earth leaching is not affected, and magnesium sulfate wastewater can be recycled.

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李向东, 陈贵青, 张瑞霞, 等. 硫酸镁废水回用稀土矿浸取工艺试验研究[J].中国有色冶金,2025,54(6):108-114.

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  • 收稿日期:2025-04-28
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  • 在线发布日期: 2025-12-26
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