Home / Publications / Journals / Nuclear Technology / Volume 77 / Number 3
Nuclear Technology / Volume 77 / Number 3 / June 1987 / Pages 299-302
Technical Paper / Chemical Processing / dx.doi.org/10.13182/NT87-A33969
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A nonlinear optimization program was used to fit the model equation to the experimental equilibrium data of a thorium-nitrate/nitric-acid-1-M di-n-heptyl sulfoxide (DHPSO) 1,1,2-trichloroethane (TCE) system successfully. The extraction equilibrium curves for this system obey Langmuir type. The product of parameters A and K is the maximum extraction distribution coefficient that can be used to compare the extraction power of 1 M DHPSO-TCE with respect to Th(NO3)4 at various aqueous acidities.