2021
DOI: 10.1007/s10967-021-07867-w
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The extraction of trivalent actinides and lanthanides by a novel unsymmetrical diglycolamide

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Cited by 5 publications
(9 citation statements)
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“…It can be seen that the extraction of Nd(III) in organic phase increases with increase in the concentration of Nd(III) in aqueous phase followed by saturation in the loading of Nd(III) in organic phase at 8 g/L (∼ 0.05 M). This value corresponds to the formation of 1 : 4 Nd(III) to D 3 DODGA complex in organic phase, which is in good agreement with the stoichiometry of trivalent Am-(III) : D 3 DODGA reported by Ravi et al [24][25][26] It is important to note from Figure 8 that there is no third phase formation in organic phase even after contacting the organic phase with aqueous solution containing 40 g/L Nd(III) in 3 M nitric acid. This value is much higher than the total amount of lanthanides and actinides (3 to 6 g/L) present in the high-level liquid waste arising from fast reactor fuel reprocessing.…”
Section: Extraction Behaviour Of Nd(iii) From Nitric Acidsupporting
confidence: 91%
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“…It can be seen that the extraction of Nd(III) in organic phase increases with increase in the concentration of Nd(III) in aqueous phase followed by saturation in the loading of Nd(III) in organic phase at 8 g/L (∼ 0.05 M). This value corresponds to the formation of 1 : 4 Nd(III) to D 3 DODGA complex in organic phase, which is in good agreement with the stoichiometry of trivalent Am-(III) : D 3 DODGA reported by Ravi et al [24][25][26] It is important to note from Figure 8 that there is no third phase formation in organic phase even after contacting the organic phase with aqueous solution containing 40 g/L Nd(III) in 3 M nitric acid. This value is much higher than the total amount of lanthanides and actinides (3 to 6 g/L) present in the high-level liquid waste arising from fast reactor fuel reprocessing.…”
Section: Extraction Behaviour Of Nd(iii) From Nitric Acidsupporting
confidence: 91%
“…In order to overcome this limitation, advanced diglycolamides like N,N-dioctyl-N',N'-didodecyl diglycolamide (D 3 DODGA) and other DGAs have been developed and studied for An(III) and Ln(III) extraction from nitric acid and simulated wastes. [24][25][26] The results revealed that D 3 DODGA does not form third phase during the extraction of trivalent metal ions from nitric acid solutions representing HLLW unlike TODGA and TEHDGA and therefore D 3 DODGA/n-DD is regarded as a promising solvent for the extraction of trivalent actinides from HLLW. In addition, a good extractant should also possess good radiation stability when it is proposed for nuclear reprocessing applications.…”
Section: Introductionmentioning
confidence: 96%
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“…7 Due to lanthanide contraction, most ligands prefer to bind heavier lanthanides than the lighter ones, because of the decreasing ion size traversing the series. Commercial extractants employ oxygen donors such as tributyl-phosphate (TBP), 8 diglycolamide (DGA), [9][10][11] and bis(2-ethylhexyl) phosphoric acid (D2EHPA). 12 Ligands with N donors such as alkylated bis-triazinyl pyridines (BTP), 13 6,6 ′ -bis-triazinyl-2,2 ′ -bipyridine (BTBP), 14 and 2,9-bistriazinyl-1,10-phenanthroline (BTPhen) 15,16 are also used.…”
Section: Introductionmentioning
confidence: 99%
“…High D values indicate better extraction efficiency and imply the formation of stable Ln­(III) complexes in the organic phase. Ligands that show great promise in REE separations include diglycolamides (DGA), alkylated bis-triazinyl pyridines (BTP), and 2,9-bis-lactam-1,10-phenanthroline (BLPhen), , among others. Extraction performance is also impacted by experimental conditions, including solvent, temperature, and volume of each phase. Organic solvents such as toluene, n-dodecane, 1-octanol, and dichloroethane are commonly used to carry out the liquid–liquid separations.…”
Section: Introductionmentioning
confidence: 99%