F. Bunus et al., SIMULTANEOUS RECOVERY AND SEPARATION OF URANIUM AND RARE-EARTHS FROM PHOSPHORIC-ACID IN A ONE-CYCLE EXTRACTION STRIPPING PROCESS, Hydrometallurgy, 35(3), 1994, pp. 375-389
A new technology for uranium and rare earth recovery from wet process
phosphoric acid (WPA) in a one-cycle extraction-stripping method was s
imple and easy to control because only acidic media were involved. The
process is based on uranium and rare earth extraction from WPA with d
i(2-ethylhexyl)phosphoric acid (DEPA) and tri-n-butylphosphate (TBP).
DEPA was found to be the only efficient, stable and easy to strip extr
actant. Other organophosphoric (acidic) esters are unstable against hy
drolysis and are difficult to strip. The stripping process is carried
out with a medium containing acidic fluoride for both rare earths and
for uranium. In the latter case uranium extracted as U (VI) is reduced
to U (IV) inextractable state by Fe(II) introduced into the stripping
solution. Both rare earths and uranium as U(IV) are instantly precipi
tated as fluorides. Uranium precipitates as UF42.5H2O or a tetravalent
compound, depending on the stripping solution. The precipitate is a '
'green cake''. The ''green cake'', with previous dehydration in nitrog
en atmosphere at 400-degrees-C, could be oxidized by F2 to hexafluorid
e, UF6, of high purity. The rare earth fraction consisted of the yttri
um group, with yttrium as the predominant element. The process describ
ed here requires lower investment costs than those of a dual extractio
n-stripping process. Operation costs involved are approximately US $ 3
0/kg for green WPA.