Rare earths from secondary sources: profitability study

V. Innocenzi, I. D. Michelis, F. Ferella, F. Vegliò
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引用次数: 12

Abstract

2016) Abstract. The paper is focused on the economic analysis of two hydrometallurgical processes for recovery of yttrium and other rare earth elements (REEs) from fluorescent phosphors of spent lamps. The first process includes leaching with sulphuric acid and precipitation of a mixture of oxalates by oxalic acid, the second one includes leaching with sulphuric acid, solvent extraction with D2EHPA, stripping by acid and recovery of yttrium and traces of other rare earths (REs) by precipitation with oxalic acid. In both cases the REEs were recovered as oxides by calcination of the oxalate salts. The economic analysis was estimated considering the real capacity of the HydroWEEE mobile’s plant (420 kg batch -1 ). For the first flow-sheet the cost of recycling comes to 4.0 € kg -1 , while the revenue from the end-product is around 5.40 € kg -1 . The second process is not profitable, as well as the first one, taking into account the composition of the final oxides: the cost of recycling comes to 5.2 € kg -1 , while the revenue from the end-product is around 3.56 € kg -1 . The process becomes profitable if the final RE oxide mixture is sold for nearly 50 € kg -1 , a value rather far from the current market prices but not so unlikely since could be achieved in the incoming years, considering the significant fluctuations of the Res’
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二次来源稀土:盈利能力研究
2016)抽象。本文对两种湿法冶金工艺从废灯荧光粉中回收钇和其他稀土元素进行了经济分析。第一个过程包括硫酸浸出和草酸沉淀草酸混合物,第二个过程包括硫酸浸出、D2EHPA溶剂萃取、酸提和草酸沉淀回收钇和微量其他稀土(REs)。在这两种情况下,稀土元素通过草酸盐的煅烧被回收为氧化物。经济分析是考虑到HydroWEEE移动装置的实际容量(420公斤批次-1)进行估计的。对于第一个流程表,回收成本为4.0欧元/千克,而最终产品的收入约为5.40欧元/千克。考虑到最终氧化物的成分,第二种方法和第一种方法一样无利可图:回收成本为5.2欧元千克-1,而最终产品的收入约为3.56欧元千克-1。如果最终的稀土氧化物混合物的售价接近50欧元千克-1,该过程就会有利可图,这个价格与目前的市场价格相差甚远,但也不是不太可能,因为考虑到稀土价格的大幅波动,在未来几年内可以实现。
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