The development of an extraction strategy based on EHEHP-type functional ionic liquid for heavy rare earth element separation
Introduction
Rare earth elements (REEs) are critical materials in many cutting-edge technology products. The economic impact of the growing scarcity of REEs has been the reason for many countries to address their strategic positions on the criticality of REEs (Eliseeva and Bünzli, 2011). Ion-adsorption mineral is the important rare earth resource in China. Unlike bastnasite and monazite, ion-adsorption mineral is enriched in HREEs (Yang et al., 2013). According to the US DOE medium-term criticality matrices, the rare earth metals (dysprosium, neodymium, terbium, europium and yttrium), are assessed as most critical because of their applications in the clean energy technologies — including wind turbines, electric vehicles, photovoltaic cells and fluorescent lighting (Bauer et al., 2010). In the five REEs mentioned above, dysprosium, terbium, yttrium are heavy rare earth elements (HREEs). According to the statistics from United States Geological Survey (Long, 2011), the global yields of HREEs are far lower than those of light rare earth elements (LREEs). Therefore, HREEs are more important than LREEs since the supply risk and importance to clean energy. 2-ethyl(hexyl) phosphonic acid mono-2-ethylhexyl ester (HEH[EHP], P507) is the most widely used extractant for individual REE separation in Chinese rare earth industry. Because of the well performance, HEH[EHP] has been applied for decades. However, some properties of HEH[EHP] for REEs separation are still unsatisfactory, such as the saponification wastewater (Wang et al., 2014). To develop efficient and environment-friendly method for HREEs separation, some separation technologies have been reported. Liao et al. (Liao et al., 2010) studied the mechanism of Cyanex272-HEH[EHP] impregnated resin for HREEs separation from hydrochloric acid solution using IR spectrometer, saturation method, and slope analysis. The HPLC method using acetic acid as novel eluent was explored for selective separation of yttrium from the HREEs (Kifle and Wibetoe, 2013). Abreu et al. (Abreu and Morais, 2014) investigated three organophosphorus acids (DEHPA, IONQUEST®801 and CYANEX®272), a mixture of DEHPA/TOPO (neutral ester) and three amines (ALAMINE®336, ALIQUAT®336 and PRIMENE®JM-T) in hydrochloric media and sulphuric media for HREEs separation.
Ionic liquids (ILs) are salts, they are generally liquid below 100 °C. Some applications of ILs at industrial scale have been established, e.g. aluminum plating in BASF, Difasol in Institut Français du Pétrole, paint additives in Degussa, hydraulic ionic liquid compressor in Linde, batteries in Pionics, and solar cells in G24i (Petkovic et al., 2011). IL-based extraction is a separation strategy that applies ILs instead of volatile organic compounds as diluents and/or extractants. The properties of ILs make them particularly suitable for solvent extraction, including their low volatility and combustibility, wide liquid range, thermal stability, adjustable functional group, high conductivity, and wide electrochemical window (Castillo et al., 2014, Sun et al., 2012a, Sun et al., 2012b, Coll et al., 2012, Tong et al., 2014). Sun et al., 2009, Sun et al., 2010 reported the inner synergistic effects between cations and anions of ABC-BILs for REEs extraction. The inner synergistic effect of ABC-BIL is a novel synergistic extraction. When the precursory extractants are prepared as ABC-BILs, their extractabilities can be increased due to the inner synergistic effect. Moreover, millions of tons of saponification wastewaters annually from acidic extractants in industrial REEs separation may be reduced by using the ABC-BILs. The achievement highlights considerable environmental value and economic value (Sun and Waters, 2014). Up to now, many interesting results concerning ABC-BILs have been reported. Wang et al., 2011 studied the extraction and separation of REEs using tricaprylmethylammonium sec-octylphenoxy acetate ([A366][CA-12]) and tricaprylmethylammonium sec-nonylphenoxy acetate ([A336][CA-100]) in chloride medium. Their results indicated that extractabilities of the bifunctional ILs were higher than those of conventional extractants, such as CA-12, CA-100, TBP, and P350. To develop efficient IL-based extraction systems, Sun et al., 2012a prepared ammonium- and phosphonium-based ILs that incorporating deprotonated di(2-ethylhexyl)phosphoric acid (HDEHP) as anion component. The anion-functionalized ILs resulted in significantly enhanced extractabilities and selectivities for REEs in TALSPEAK-like process. Rout et al., 2013 studied some ILs with bis(2-ethylhexyl)phosphate anion ([DEHP]−), i.e., [C6mim][DEHP], [C6mpyr][DEHP] and [N4444][DEHP] for Nd(III) extraction from nitric acid medium. The cations of ILs were indicated to have distinct influences on the extraction properties of extractants. It was possible to tune the extractability and selectivity of metal ion by a proper choice of IL cation. Castillo et al., 2014 removed Cu(II) from highly contaminated aqueous solutions (1000 mg/L Cu(II)) by quaternary ammonium type ionic liquid [A336/Cy272] in sulfate, chloride or mixed media, with extraction efficiencies up to 95%. In this paper, we first investigate the extraction and separation performances of EHEHP type ABC-BIL for neighboring HREEs.
Section snippets
Reagents and chemicals
Trioctylmethylammonium bromide ([N1888]Br) were purchased from Yixing Kai Lida Chemical Co., Ltd. (China). An anion-exchange resin (Dowex Monosphere 550A (OH)) was obtained from the Dow Chemical Company. HEH[EHP] was supplied by Luoyang Aoda Chemical Co., Ltd. (China). The extractant was purified by washing with 2% Na2CO3, 0.2 mol/L H2SO4 and distilled water, respectively. 1H and 13C nuclear magnetic resonance (NMR) spectra were obtained in CDCl3 with an AV III-500 BRUKER spectrometer. The
The extractabilities of HEH[EHP], mixed [N1888]Br and HEH[EHP], [N1888][EHEHP] for REEs
In this section, we compared the distribution ratios of HEH[EHP], mixed [N1888]Br and HEH[EHP], [N1888][EHEHP] for REEs. As shown in Fig. 2, extractabilities of the systems for individual HREE (yttrium group) increase gradually as atomic numbers of the REEs increased. Although HEH[EHP] were uniformly common in the three extracting systems, extractabilities of the systems were quite different. Distribution coefficient sequence of the extracting systems for REEs was [N1888][EHEHP] > HEH[EHP] > mixed
Conclusions
In summary, HEH[EHP] is one of the most widely used extractants in Chinese ion-adsorption REE mineral separation industry. However, HEH[EHP] needs to be saponified for REE separation. The saponified HEH[EHP] releases millions of tons of saponification wastewater annually. To develop sustainable and efficient separation technology for HREEs, HEH[EHP] were prepared as ABC-BIL by acid–base neutralization method in this paper. The prepared EHEHP type ABC-BIL ([N1888][EHEHP]) was first investigated
Acknowledgements
This work was supported by ‘Hundreds Talents Program’ from Chinese Academy of Sciences, National Natural Science Foundation of China (21571179), Science and Technology Major Project of Fujian Province and ‘Xiamen Double Hundred Plan’.
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