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U.S. Department of Energy
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Thermodynamic modeling of chemical equilibria in metal extraction. [PUREX, TRUEX solvents]

Conference ·
OSTI ID:5372281
Models of equilibrium extraction data are being developed for use in computer simulations of metal extraction processes. The correlations are based on chemical mass action principles in which the effects of metal complexation and aqueous phase activity coefficients are considered. Activity coefficients in mixed electrolyte solutions at high ionic strengths are calculated using methods available in the literature. This modeling approach is demonstrated for HNO/sub 3/ extraction with both the PUREX and TRUEX solvents and for Am/sup 3 +/ extraction by octyl-phenyl-N,N-diisobutylcarbamoylmethylphosphine oxide, which is the primary extractant in the TRUEX solvent. 23 refs., 4 figs., 4 tabs.
Research Organization:
Argonne National Lab., IL (USA)
DOE Contract Number:
W-31109-ENG-38
OSTI ID:
5372281
Report Number(s):
CONF-871016-1; ON: DE88006006
Country of Publication:
United States
Language:
English