Solvent extraction of Eu(III) from hydrochloric acid solutions using PC88A and Cyanex 572 in kerosene

被引:25
作者
Agarwal, V [1 ]
Safarzadeh, M. S. [1 ]
Bendler, J. T. [1 ]
机构
[1] South Dakota Sch Mines & Technol, Dept Mat & Met Engn, 501 East St Joseph St, Rapid City, SD 57701 USA
关键词
Solvent extraction; Europium; PC88A; Cyanex; 572; Infrared spectrum; Molecular modeling; RARE-EARTH-ELEMENTS; SEPARATION; YTTRIUM; ION;
D O I
10.1016/j.hydromet.2018.03.011
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
Solvent extractions of europium (Eu(III)) from hydrochloric acid solutions using 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester (PC88A) and Cyanex 572 (chemical structure not reported) diluted in kerosene are compared and discussed. Pourbaix and speciation diagrams for Eu(III) in chloride solutions are presented to clarify the chemistry of solution at different acidities and chloride concentrations. Preliminary structures, energies and free energies of Eu(III) species in both aqueous and organic phases (the latter consisting of phosphonic acid in heptane) were calculated and compared using molecular modeling. The effects of pH (1-5), extractant concentration (1-100 mM) and ionic strength (0,05-1 M) are studied to systematically characterize the extraction behavior of Eu(III) and, based on these results, an extraction mechanism is suggested. It is found that under similar experimental conditions a higher extent of extraction is obtained with PC88A compared with Cyanex 572. The infrared spectra of the loaded organic solutions support the hypothesis that the Eu(III) extraction reaction is driven by a cation exchange mechanism. Separation studies of Eu(III) from other rare earth elements (REEs) were also carried out and revealed that PC88A provides higher separation of Eu(III) from light REEs while Cyanex 572 achieves higher separation from heavy REEs.
引用
收藏
页码:152 / 160
页数:9
相关论文
共 22 条
[1]   Solvent extraction and separation of cerium(III) and samarium(III) from mixed rare earth solutions using PC88A [J].
Agarwal, V. ;
Safarzadeh, M. S. .
MINERALS & METALLURGICAL PROCESSING, 2017, 34 (03) :125-131
[2]  
[Anonymous], 2011, CRITICAL MAT STRATEG
[3]  
[Anonymous], 2009, GAUSSIAN 09 REVISION
[4]  
Bauer D., 2010, U.S. Department of Energy critical materials strategy
[6]  
Cytec, 2014, CYAN 572 SOLV EXTR R
[7]   Thermodynamic and Structural Features of Aqueous Ce(III) [J].
Dinescu, Adriana ;
Clark, Aurora E. .
JOURNAL OF PHYSICAL CHEMISTRY A, 2008, 112 (44) :11198-11206
[8]   ENERGY-ADJUSTED PSEUDOPOTENTIALS FOR THE RARE-EARTH ELEMENTS [J].
DOLG, M ;
STOLL, H ;
SAVIN, A ;
PREUSS, H .
THEORETICA CHIMICA ACTA, 1989, 75 (03) :173-194
[9]   Separation of middle rare earths by solvent extraction using 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester as an extractant [J].
Fontana, Danilo ;
Pietrelli, Loris .
JOURNAL OF RARE EARTHS, 2009, 27 (05) :830-833
[10]   Equilibrium analysis of solvent extraction of yttrium (III) and europium (III) from hydrochloric acid with P507 [J].
Fu Nian-xin ;
Sui Zhi-tong ;
Tanaka, Mikiya .
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA, 2011, 21 (09) :2093-2098