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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 />

125

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