Counter current extraction separation of rare earth traces

1976 ◽  
Vol 30 (2) ◽  
pp. 361-368 ◽  
Author(s):  
B. Tomažič ◽  
M. Branica
Molecules ◽  
2022 ◽  
Vol 27 (2) ◽  
pp. 557
Author(s):  
Sergei I. Stepanov ◽  
Nguyen Thi Yen Hoa ◽  
Ekaterina V. Boyarintseva ◽  
Alexander V. Boyarintsev ◽  
Galina V. Kostikova ◽  
...  

The article presents data on the solvent extraction separation of rare-earth elements (REEs), such as La(III), Ce(III), Pr(III), and Nd(III), using synergic mixtures of methyltrioctylammonium nitrate (TOMANO3) with tri-n-butyl phosphate (TBP) from weakly acidic nitrate solutions. Specifically, experimental results on separation of REEs, for the pair Ce(III)/Pr(III) for quaternary mixtures of REEs (La(III), Ce(III), Pr(III), Nd(III)) and for the pair La(III)/Pr(III) for solutions containing La(III), Pr(III), and Nd(III), are presented. It was shown that effective separation for the pair Ce(III)/Pr(III) from a solution containing 219 g Ce(III)/L, 106 g La(III)/L, 20 g Pr(III)/L, 55 g Nd(III)/L, and 0.1 mol/L HNO3, was achieved using 56 steps of a multistage, counter-current solvent extraction cascade with scrubbing, at an organic-to-aqueous phase volume ratio (O/A) equal to 2/1 on the extraction section and O/A equal to 4/1 on the scrubbing section, using 3.3 mol/L solutions of the mixture TOMANO3-TBP with molar ratio 0.15:0.85 in dodecane. Separation for the pair La(III)/Pr(III) could be achieved using a solvent extraction cascade with scrubbing in 32 steps at O/A equal to 2/1 on the extraction section and O/A equal to 2.8/1 on the scrubbing section of the solvent extraction cascade from a solution containing 258 g La(III)/L, 58 g Pr(III)/L, 141 g Nd(III)/L, and 0.1 mol/L HNO3 with 3.0 mol/L solution of the mixture TOMANO3-TBP with molar ratio 0.2:0.8 in dodecane.


Author(s):  
Nurul Ain Ismail ◽  
Mohd Aizudin Abd Aziz ◽  
Anwaruddin Hisyam ◽  
Mohammad Alwi Abidin

1991 ◽  
Vol 538 (1) ◽  
pp. 133-140 ◽  
Author(s):  
Eiichi Kitazume ◽  
Molina Bhatnagar ◽  
Yoichiro Ito

Author(s):  
Enxiang Liang ◽  
Xin Yang ◽  
Caixia Yang ◽  
Jianming Yi* ◽  
Qiong Wan*

1963 ◽  
Vol 84 (3) ◽  
pp. 263-267,A18 ◽  
Author(s):  
Tsunenobu SHIGEMATSU ◽  
Masayuki TABUSHI ◽  
Masakazu MATSUI ◽  
Yasuharu NISHIKAWA ◽  
Shiro GODA

2016 ◽  
Vol 80 (1) ◽  
pp. 63-76 ◽  
Author(s):  
G. A. Moldoveanu ◽  
V. G. Papangelakis

AbstractContinuous development of advanced technologies has created increasing demand for rare-earth elements (REE), with global emphasis on identifying new alternate sources to ensure adequate supply. Ore deposits containing physically adsorbed lanthanides are substantially lower grade than other REE deposit types; however, the low mining and processing costs make them economically attractive as sources of REE. To evaluate the commercial potential for the recovery of REEs from ion-adsorption deposits in a systematic manner, a standardized procedure for REE leaching was developed previously. Using this procudure it was found that, regardless of variations in ore origin and REE content, all REE consistently reached peak extraction levels under ambient conditions with fast kinetics. Various techniques to improve the REE extraction through process variations were also investigated: it was found that decreasing the L:S ratio, re-using leachate on fresh ores and counter-current leaching were all capable of increasing REE concentrations in the resultant leachate, albeit at the expense of REE extraction levels. In addition, the water content trapped in the leached material was found to contain significant amounts of REE and residual lixiviant requiring thorough washing of the solid residue.


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