DIAMEX counter-current extraction process for recovery of trivalent actinides from simulated high active concentrate

被引:122
作者
Modolo, Giuseppe [1 ]
Vijgen, Hendrik
Serrano-Purroy, Daniel
Christiansen, Birgit
Malmbeck, Rikard
Sorel, Christian
Baron, Pascal
机构
[1] Forschungszentrum Julich GmbH FZJ, Inst Safety Res & Reactor Technol, D-52425 Julich, Germany
[2] European Commiss, JRC, Inst Transuranium Elements, Karlsruhe, Germany
[3] CEA, DRCP, SCPS, Bagnols Sur Ceze, France
关键词
solvent extraction; DIAMEX process; DMDOHEMA; minor actinides; partitioning;
D O I
10.1080/01496390601120763
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
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.
引用
收藏
页码:439 / 452
页数:14
相关论文
共 16 条
[1]  
[Anonymous], 2004, TECHN REP SER
[2]  
Baron P., 2003, P GLOB 2003 NEW ORL
[3]   Diamex process for minor actinide partitioning: Hydrolytic and radiolytic degradations of malonamide extractants [J].
Berthon, L ;
Morel, JM ;
Zorz, N ;
Nicol, C ;
Virelizier, H ;
Madic, C .
SEPARATION SCIENCE AND TECHNOLOGY, 2001, 36 (5-6) :709-728
[4]  
BLANC P, P GLOB 2005 TSUK JAP
[5]  
Courson O, 2000, RADIOCHIM ACTA, V88, P857, DOI 10.1524/ract.2000.88.12.857
[6]  
Dinh B., 1992, EUR S COMP AID PROC
[7]   Transient- and steady-state concentration profiles in a DIAMEX-like countercurrent process for an(III)+Ln(III) separation [J].
Facchini, A ;
Amato, L ;
Modolo, G ;
Nannicini, R ;
Madic, C ;
Baron, P .
SEPARATION SCIENCE AND TECHNOLOGY, 2000, 35 (07) :1055-1068
[8]   6,6′-bis (5,5,8,8-tetramethyl-5,6,7,8-tetrahydro-benzo[1,2,4]triazin-3-yl) [2,2′]bipyridine, an effective extracting agent for the separation of americium(III) and curium(III) from the lanthanides [J].
Geist, Andreas ;
Hill, Clement ;
Modolo, Giuseppe ;
Foreman, Mark R. St. J. ;
Weigl, Michael ;
Gompper, Klaus ;
Hudson, Michael J. .
SOLVENT EXTRACTION AND ION EXCHANGE, 2006, 24 (04) :463-483
[9]  
Hill C., 2002, J. Nucl. Sci. Technol, V39, P309, DOI [10.1080/00223131.2002.10875470, DOI 10.1080/00223131.2002.10875470]
[10]  
Madic C., 2004, 6066 CEA