2020
DOI: 10.1016/j.seppur.2019.116429
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Recovery of neodymium and praseodymium from nitrate-based leachate of permanent magnet by solvent extraction with trioctylphosphine oxide

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Cited by 35 publications
(12 citation statements)
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“…Solvent extraction is a standard process currently employed for the removal of REEs from acidic leachates [ 18 , 19 , 20 , 21 ], especially for solutions containing high metal concentrations. Most of these highly efficient extractants are based on phosphorus reagents such as alkyl phosphate [ 19 , 22 , 23 , 24 , 25 , 26 ], alkyl phosphoric acid [ 27 , 28 , 29 ], alkyl phosphine oxide [ 30 , 31 ], phosphonium ionic liquids [ 32 , 33 ] and organophosphonic extractants [ 34 , 35 , 36 , 37 ]. The strong affinity of phosphorus-based extractants for rare earth easily explains that a strong effort has been made for designing synthetic resins bearing phosphorus-based reactive groups such as Tulsion CH-96 and T-PAR resins [ 38 , 39 ], Tulsion CH-93 [ 34 ], Purolite S957 and Diphonix [ 40 ] or metal-organic frameworks [ 41 ].…”
Section: Introductionmentioning
confidence: 99%
“…Solvent extraction is a standard process currently employed for the removal of REEs from acidic leachates [ 18 , 19 , 20 , 21 ], especially for solutions containing high metal concentrations. Most of these highly efficient extractants are based on phosphorus reagents such as alkyl phosphate [ 19 , 22 , 23 , 24 , 25 , 26 ], alkyl phosphoric acid [ 27 , 28 , 29 ], alkyl phosphine oxide [ 30 , 31 ], phosphonium ionic liquids [ 32 , 33 ] and organophosphonic extractants [ 34 , 35 , 36 , 37 ]. The strong affinity of phosphorus-based extractants for rare earth easily explains that a strong effort has been made for designing synthetic resins bearing phosphorus-based reactive groups such as Tulsion CH-96 and T-PAR resins [ 38 , 39 ], Tulsion CH-93 [ 34 ], Purolite S957 and Diphonix [ 40 ] or metal-organic frameworks [ 41 ].…”
Section: Introductionmentioning
confidence: 99%
“…The results for initial Nd concentration of 0.05 M were not used as the maximum workable TOPO Yang et al [30] found maximum extraction percentages of 80 % at a Nd:TOPO ratio of 1:350, whereas in the current study similar extraction percentages are achieved at a 1:5 ratio only. Rho et al [31] investigated extractions using the same extractant and initial Nd concentrations as those here but with kerosene as the organic solvent. The extraction percentage is plotted in Fig.…”
Section: Equilibrium Studies and Mechanism Of Extractionmentioning
confidence: 99%
“…Considering the instable supply chain of REEs, such as Nd and Dy, which are core constituents of NdFeB magnets, recovering REEs from end-of-life magnets is an essential way to decrease the supply risk . Various metallurgical processes were carried out to separate and recover the REEs from the spent NdFeB magnets, including hydrometallurgy, pyrometallurgy, chlorinated metallurgy, , electrochemistry, solvometallurgy, liquid metal extraction, and membrane separation. , …”
Section: Introductionmentioning
confidence: 99%