We report on the separation and recovery of scandium(III)
from sulfate solutions using solvent extraction and a membrane transport
system utilizing newly synthesized amic acid extractants. Scandium(III)
was quantitatively extracted with 50 mmol dm–3N-[N,N-di(2-ethylhexyl)aminocarbonylmethyl]glycine
(D2EHAG) or N-[N,N-di(2-ethylhexyl)aminocarbonylmethyl]phenylalanine (D2EHAF) in n-dodecane at pH 2 and easily stripped using a 0.5 mol dm–3 sulfuric acid solution. The extraction mechanisms
of scandium(III) extraction with D2EHAG and D2EHAF were examined,
and it was established that scandium(III) formed a 1:3 complex with
both extractants (HR), that is, Sc(SO4)2–aq + 1.5(HR)2org ⇄ Sc(SO4)R(HR)2org + H+aq + SO42–aq. The equilibrium constants
of extraction were evaluated to be 4.87 and 9.99 (mol dm–3)0.5 for D2EHAG and D2EHAF, respectively. D2EHAG and D2EHAF
preferentially extracted scandium(III) with a high selectivity compared
to common transition metal ions under high acidic conditions (0 <
pH ≤ 3). In addition, scandium(III) was quantitatively transported
from a feed solution into a 0.5 mol dm–3 sulfuric
acid receiving solution through a polymer inclusion membrane (PIM)
containing D2EHAF as a carrier. Scandium(III) was completely separated
thermodynamically from nickel(II), aluminum(III), cobalt(II), manganese(II),
chromium(III), calcium(II), and magnesium(II), and partially separated
from iron(III) kinetically using a PIM containing D2EHAF as a carrier.
The initial flux value for scandium(III) (J0,Sc = 1.9 × 10–7 mol m–2 s–1) was two times higher than that of iron(III) (J0,Fe = 9.3 × 10–8 mol
m–2 s–1).