Stetson Caleb, Prodius Denis, Lee Hyeonseok, Orme Christopher, White Byron, Rollins Harry, Ginosar Daniel, Nlebedim Ikenna C, Wilson Aaron D
Critical Materials Institute, Idaho National Laboratory, 1955 N Fremont Ave, Idaho Falls, ID, 83415, USA.
Critical Materials Institute, Ames Laboratory, US Department of Energy, Ames, IA, 50011-3020, USA.
Nat Commun. 2022 Jul 1;13(1):3789. doi: 10.1038/s41467-022-31499-7.
This work reports a dimethyl ether-driven fractional crystallization process for separating rare earth elements and transition metals. The process has been successfully applied in the treatment of rare earth element-bearing permanent magnet leachates as an atom-efficient, reagent-free separation method. Using ~5 bar pressure, the solvent was dissolved into the aqueous system to displace the contained metal salts as solid precipitates. Treatments at distinct temperatures ranging from 20-31 °C enable crystallization of either lanthanide-rich or transition metal-rich products, with single-stage solute recovery of up to 95.9% and a separation factor as high as 704. Separation factors increase with solution purity, suggesting feasibility for eco-friendly solution treatments in series and parallel to purify aqueous material streams. Staged treatments are demonstrated as capable of further improving the separation factor and purity of crystallized products. Upon completion of a crystallization, the solvent can be recovered with high efficiency at ambient pressure. This separation process involves low energy and reagent requirements and does not contribute to waste generation.
本工作报道了一种用于分离稀土元素和过渡金属的二甲醚驱动分步结晶过程。该过程已成功应用于含稀土元素的永磁体浸出液的处理,是一种原子高效、无需试剂的分离方法。在约5巴的压力下,将溶剂溶解到水体系中,使所含金属盐以固体沉淀的形式析出。在20至31°C的不同温度下进行处理,可使富含镧系元素或富含过渡金属的产物结晶,单级溶质回收率高达95.9%,分离因子高达704。分离因子随溶液纯度的提高而增加,这表明串联和并联进行环保溶液处理以净化水性物料流具有可行性。分步处理证明能够进一步提高结晶产物的分离因子和纯度。结晶完成后,溶剂可在常压下高效回收。这种分离过程所需的能量和试剂较少,且不会产生废物。