COMPLETE DOCUMENT (1862 kb) - OECD Nuclear Energy Agency
COMPLETE DOCUMENT (1862 kb) - OECD Nuclear Energy Agency
COMPLETE DOCUMENT (1862 kb) - OECD Nuclear Energy Agency
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Figure II.6 DIAMEX process<br />
Feed solution<br />
(3-5 M HNO 3)<br />
Diamide<br />
solvent<br />
Rinse<br />
U, Pu, Am,<br />
Cm, Ln(III)<br />
extraction<br />
FP solution<br />
HNO 3 (0.1 M)<br />
An(III) + Ln(III)<br />
stripping<br />
An + Ln solution<br />
An/Ln<br />
Separation<br />
Complexant or<br />
reductant<br />
(to be defined)<br />
U, Pu<br />
stripping<br />
U, Pu, solution<br />
Solvent<br />
treatment<br />
Selective extraction of actinides<br />
Tripyridyltriazine (TPTZ)<br />
Tripyridyltriazine ligand (TPTZ) is a terdendate nitrogen-donor ligand which can selectively<br />
extract An(III) from An+Ln mixtures when used in synergistic combination with an organic cation<br />
exchanger. This system was first studied in the 80s by Vitorge [17]. Good separation factors were<br />
obtained for An(III) vs Ln(III) using TPTZ+HDNNS (di-nonylnaphthalenesulfonic acid) or TPTZ +<br />
alpha-bromocapric acid. Tests of the process using synthetic spiked solutions were successfully<br />
conducted at Fontenay-aux-Roses Research Centre. Improvements to the process are underway in a<br />
European research programme. One way to improve the system is to use the lipophilic alkyl derivative<br />
of TPTZ developed jointly by the University of Reading (UK) and the CEA (France). Recently, Kolarik<br />
et al. at the FZK (Germany) designed a very efficient family of molecules related to TPTZ able to<br />
extract selectively An(III) over Ln(III) from aqueous nitric acid solution [18].<br />
CYANEX 301<br />
Zhu et al. in Tsinghua University (China) recently published extraordinary results for the<br />
separation of An(III) over Ln(III) using CYANEX 301 extractant [19]. CYANEX 301 consists chiefly<br />
of bis (2,4,4-trimethylpentyl) dithiophosphinic acid. The commercial product contains many impurities<br />
some of which are detrimental to the extraction of metal ions, and especially to the separation of An(III)<br />
over Ln(III). In the case of crude CYANEX 301, no An/Ln separation is observed unless the extractant<br />
is saponified (i.e. neutralised with an alkali). In this case, very high An(III)/Ln(III) separation factors<br />
can be obtained. After purification of CYANEX 301 by precipitation of its ammonium salt, there is no<br />
need for saponification of the extractant to obtain tremendously high An(III)/Ln(III) separation factors,<br />
up to 5 900. Nevertheless, one of the drawbacks in using CYANEX 301 for An/Ln separation is the<br />
fact that the aqueous solution must be adjusted to a rather high pH of 3.5 to 4.<br />
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