Journal
SEPARATION SCIENCE AND TECHNOLOGY
Volume 42, Issue 3, Pages 439-452Publisher
TAYLOR & FRANCIS INC
DOI: 10.1080/01496390601120763
Keywords
solvent extraction; DIAMEX process; DMDOHEMA; minor actinides; partitioning
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The partitioning of trivalent actinides was demonstrated with a new version of the French DIAMEX (DIAMide EXtraction) process. A continuous counter-current experiment using a 16-stage centrifugal extractor battery was tested using 1 mol/L N,N'-dimethyl-N,N'-dioctyl-hexylethoxy-malonamide (DMDOHEMA) in TPH as the extractant. A high active concentrate (HAC), obtained after concentration and denitration of a high active raffinate (HAR) with a concentration factor of 10, was used as a feed. Based on results from cold and hot batch extraction experiments and computer code calculations, a flowsheet was developed and a full test was carried out using a simulated HAC solution spiked with radionuclides (Am-241, Cm-244, Eu-152, and Cs-134). In the DIAMEX process, five extraction stages were sufficient to obtain Am and Cm (feed/raffinate) greater than 5000 and for the coextracted lanthanides decontamination factors between 1100 and 4500. Co-extraction of zirconium, molybdenum, and palladium was prevented by using oxalic acid and HEDTA. The back extraction comprising 4 stages was also efficient and the recoveries of actinides were greater than 99.8%, which can be further improved by a minor process flowsheet optimisation. The experimental steady-state concentration profiles of important solutes were determined and compared with model calculations and good agreement was generally obtained.
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