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Leaching of rare earth elements from waste lamp phosphor mixtures by reduced alkali fusion followed by acid leaching

机译:通过减少碱熔和酸浸从废灯磷光体混合物中浸出稀土元素

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Because of the complex crystal structures of the blue powder and green powder in waste rare earth phosphor powder and the relative high content of Ce and Tb, efficient extraction of rare earth elements (REEs) is difficult. The highest leaching efficiency of REEs is only about 90% with present processes, and utilization of the REEs is low. To improve the leaching efficiency of waste rare earth phosphor, a novel process of reduced alkali fusion followed by acid leaching to recover REEs from waste phosphor powder is proposed. Under the conditions of mass ratio of reductive iron powder to waste rare earth phosphor of 1:200, alkali to phosphor mass ratio of 2:1, alkali fusion temperature of 700 degrees C, alkali fusion time of 3 h, hydrochloric acid concentration of 3 mol L-1, liquid to solid ratio (v/w) of 7.5:1, acid leaching temperature of 70 degrees C, and acid leaching time of 1 h, the total leaching efficiency of REEs is as high as 99.35%, and the leaching efficiencies of Ce, Eu, Tb, and Y are 98.12%, 99.93%, 99.37%, and 99.60%, respectively. The results indicate that the REEs in waste phosphor powder can be efficiently recovered by the proposed process. (C) 2016 Elsevier B.V. All rights reserved.
机译:由于废稀土磷光体粉末中蓝色粉末和绿色粉末的复杂晶体结构以及相对较高的Ce和Tb含量,很难高效提取稀土元素(REEs)。在目前的工艺中,稀土元素的最高浸出效率仅为约90%,并且稀土元素的利用率低。为了提高废稀土荧光粉的浸出效率,提出了一种减少碱熔,然后进行酸浸从废荧光粉中回收稀土元素的新方法。在还原铁粉与废稀土荧光粉的质量比为1:200,碱与荧光粉的质量比为2:1,碱熔温度为700摄氏度,碱熔时间为3小时,盐酸浓度为3的条件下mol L-1,液/固比(v / w)为7.5:1,酸浸温度为70℃,酸浸时间为1 h,REEs的总浸出效率高达99.35%,且Ce,Eu,Tb和Y的浸出效率分别为98.12%,99.93%,99.37%和99.60%。结果表明,所提出的方法可以有效地回收废荧光粉中的稀土元素。 (C)2016 Elsevier B.V.保留所有权利。

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