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COMPLETE DOCUMENT (1862 kb) - OECD Nuclear Energy Agency

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thus preventing its dispersion in the downstream operations where its controlled management would be<br />

quite difficult.<br />

The operating conditions of fuel dissolution are selected to ensure that the iodine is brought to<br />

and maintained in the elemental state, and to entrain it in the off-gas. The iodine is recovered in an<br />

aqueous solution by caustic scrub of the off-gas.<br />

This specific effluent of iodine, which is discharged into the sea today, thus contains nearly all<br />

the iodine initially present in the irradiated fuel. Some reprocessing plants envisage the use of iodine<br />

immobilisation by adsorption on silver impregnated zeolites.<br />

Other long-lived fission products<br />

As to the other long-lived fission products, it is clear that the PUREX process cannot be used<br />

to separate caesium and strontium, since these mono- and divalent elements are unextractable by TBP.<br />

The behaviour in the PUREX process of the other fission products which have long-lived isotopes (Pd,<br />

Se, Sn) is not precisely known. A combined electrolytic extraction of Pd 2+ with the other platinum group<br />

elements (RuNO 3+ , Rh 3+ −<br />

) and TcO 4<br />

2−<br />

(and probably SeO 4<br />

) seems to be promising from even higher<br />

acidic PUREX liquors [1].<br />

1.1.1.3 Long-lived activation products<br />

The activation products formed in the fuel element structural metals (stainless steels, inconel<br />

and zircaloy) mostly remain in these materials and are found in the corresponding “hulls and end pieces”<br />

waste stream. The 14 C issue should receive increasing attention because of this isotope’s impact on the<br />

biosphere.<br />

1.1.1.4 Conclusions<br />

The behaviour of the minor actinides and long-lived fission products in the PUREX process<br />

can be divided into three categories:<br />

• elements already partially separated by the PUREX process: neptunium, technetium and<br />

iodine. For these elements, the R&D objective involves process extensions to achieve the<br />

desired separation performance. This first aspect is discussed further in Section 1.1.2.<br />

• elements separable by TBP, for which a complementary step to the present PUREX<br />

process can be developed. This applies to zirconium.<br />

• elements that cannot be separated by the PUREX process:<br />

– americium and curium,<br />

– caesium, strontium and probably the other fission products (Pd, Se, Sn).<br />

To separate these elements, it is necessary to develop new classes of extractants, or to resort<br />

to different separation methods. The corresponding developments are discussed in Section 1.1.3 (Am<br />

and Cm) and Section 1.1.4 (FPs).<br />

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