Trivalent Lanthanide/Actinide Separation Using Aqueous-Modified TALSPEAK Chemistry

Travis S. Grimes, Richard D. Tillotson, Leigh R. Martin

Research output: Contribution to journalArticlepeer-review

27 Scopus citations

Abstract

TALSPEAK is a liquid/liquid extraction process designed to separate trivalent lanthanides (Ln3+) from the minor actinides (MAs) Am3+ and Cm3+. Traditional TALSPEAK organic phase is comprised of the monoacidic dialkyl bis(2-ethylhexyl)phosphoric acid extractant (HDEHP) in diisopropyl benzene (DIPB). The aqueous phase contains a soluble aminopolycarboxylate diethylenetriamine-N,N,N',N",N"-pentaacetic acid (DTPA) in a concentrated (1.0-2.0 M) lactic acid (HL) buffer with the aqueous acidity typically adjusted to pH 3.0. This process balances the selective complexation of the actinides by DTPA against the electrostatic attraction of the lanthanides by the HDEHP extractant to achieve the desired trivalent lanthanide/actinide group separation. In this study, the aqueous phase has been modified by replacing the lactic acid buffer with a variety of simple and longer-chain amino acid buffers. The results show successful trivalent lanthanide/actinide group separation with the aqueous-modified TALSPEAK process at pH 2. The amino acid buffer concentrations were reduced to 0.5 M (at pH 2), and separations were performed without any effect on phase-transfer kinetics. Successful modeling of the aqueous-modified TALSPEAK process (p[H+] 1.6-3.1) using a simplified thermodynamic model and an internally consistent set of thermodynamic data is presented.

Original languageEnglish
Pages (from-to)378-390
Number of pages13
JournalSolvent Extraction and Ion Exchange
Volume32
Issue number4
DOIs
StatePublished - Jun 2014

Keywords

  • HDEHP
  • Solvent extraction
  • actinide lanthanide separations
  • amino acids

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