SIMULTANEOUS RECOVERY AND SEPARATION OF URANIUM AND RARE-EARTHS FROM PHOSPHORIC-ACID IN A ONE-CYCLE EXTRACTION STRIPPING PROCESS

Citation
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
Citations number
14
Categorie Soggetti
Metallurgy & Mining
Journal title
ISSN journal
0304386X
Volume
35
Issue
3
Year of publication
1994
Pages
375 - 389
Database
ISI
SICI code
0304-386X(1994)35:3<375:SRASOU>2.0.ZU;2-8
Abstract
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.