Solvent Extraction and Ion Exchange · 2014 · 35 citations · 11 references
Solvent ExtractionChemical EngineeringChemical KineticsTrivalent ActinidesEngineeringSeparation ScienceExtraction RateSeparation TechnologyOrganic ChemistryAnalytical ChemistrySeparation TechniqueChemistryAdvanced SeparationProcess Chemistry
A method for separating the trivalent actinides and lanthanides is being developed using 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester (HEH[EHP]) as the extractant. The method is based on the preferential binding of the actinides in the aqueous phase by N-(2-hydroxyethyl)ethylenediamine-N,N',N'-triacetic acid (HEDTA), which serves to keep the actinides in the aqueous phase while the lanthanides are extracted into an organic phase containing HEH[EHP]. The process is very robust, showing little dependence upon the pH or the HEH[EHP], HEDTA, and citrate concentrations over the ranges that might be expected in a nuclear fuel recycling plant. Single-stage runs with a 2-cm centrifugal contactor indicate that modifications to the process chemistry may be needed to increase the extraction rate for Sm, Eu, and Gd. The hydraulic properties of the system are favorable to application in centrifugal contactors.
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B. Weaver, F.A. Kappelmann · Journal of Inorganic and Nuclear Chemistry · 1968 · 213 citations
Solvent Extraction, Chemical Engineering, Trivalent Actinides +12