Demonstration of a TODGA based Extraction Process for the Partitioning of Minor Actinides from a PUREX Raffinate
Journal article, 2009

Efficient recovery of minor actinides (MA) from genuine PUREX raffinate has been successfully demonstrated by the TODGA + TBP extractant mixture dissolved in an industrial aliphatic solvent TPH. The process was carried out in centrifugal contactors using an optimized flow-sheet involving a total of 32 stages, divided into 4 stages for extraction, 12 stages for scrubbing and 16 stages for back-extraction. Very high feed decontamination factors were obtained (Am, Cm 40 000) and the recovery of these elements was higher than 99.99%. Of the non-lanthanide fission products only Y and a small part of Ru were co-separated into the product fraction together with the lanthanides and the MA.

TODGA process

waste

recovery

diamex process

americium

lanthanides

Solvent extraction

minor actinides

partitioning

Author

Daniel Magnusson

Chalmers, Chemical and Biological Engineering, Nuclear Chemistry

B. Christiansen

Joint Research Centre (JRC), European Commission

J. P. Glatz

Joint Research Centre (JRC), European Commission

R. Malmbeck

Joint Research Centre (JRC), European Commission

G. Modolo

Forschungszentrum Jülich

D. Serrano-Purroy

Joint Research Centre (JRC), European Commission

C. Sorel

The French Alternative Energies and Atomic Energy Commission (CEA)

Solvent Extraction and Ion Exchange

0736-6299 (ISSN) 1532-2262 (eISSN)

Vol. 27 1 26-35

DOI

10.1080/07366290802544726

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