The extraction of Th 4+ and UO 2 2+ from an aqueous phase into a solution of bis 2-ethylhexyl phosphoric acid, (2-C 2H 5·C 6H 12O) 2PO(OH), HDEHP, in the monomerizing diluent 2-ethylhexanoic acid has been studied in terms of the concentration of hydrogen ion in the equilibrated aqueous phase and of HDEHP in the opposing equilibrated organic phase. The extraction stoichiometries, with the corresponding expression for K in terms of F (the formality of HDEHP in the organic phase), [H +] (the concentration of hydrogen ion in the aqueous phase), and K s , for a 1.00 F (NaCl + HCl) aqueous phase, are: Th A 4++ 5HY O⇄ Th(HYO O+ 4H A + K = K sF 5 [H +] 4 UO 2A 2+ + 3HY O ⇄ UO 2( HY 3) O+ 2H A + K = K sF 3 [H +] 2 where HY represents the monomer of HDEHP and the formulations of extracted species are non committal with respect to structure. With HZ representing the monomer of 2-ethylhexanoic acid, suggested formulations of the extracted species in terms of homogeneous and heterogeneous dimers are: Th(HY 2)(HYZ) 3 and UO 2(HY 2)(HYZ). The K s values are: Th 4+ (7 × 10 4) and UO 2 2+ (2 × 10 2). Comparison of the extraction of Th 4+ and UO 2 2+ with the extraction, previously reported, of Am 3+, Eu 3+, Tm 3+ and Y 3+ in the same system is made. Application (patented) of this liquid-liquid extraction system to the purification of thorium from contaminant rare earths and yttrium is demonstrated.
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