The recovery of metals using solvent extraction can offer
significant environmental advantages over energy- and capital-
intensive pyrometallurgical routes, especially if a single
metal is targeted.[7] Selectivity of extraction is achieved by
designing a reagent that favors the phase transfer of one metal
from a mixed-metal aqueous leach solution to an organic
phase.[8] Currently, 25% of global Cu recovery is carried out
by hydrometallurgy using phenolic oxime reagents,[8] the
development of which relied on an understanding of the
coordination and supramolecular chemistry of copper.
In contrast, the chemistry that underpins the recovery of
gold by solvent extraction is poorly understood. Commercial
reagents such as MIBK (isobutyl methyl ketone), DBC
(diethylene glycol butyl ether), and 2-EH (2-ethylhexanol)
recover gold as its metalate (AuCl4)- from aqueous HCl by
solvent extraction (Eq. (1)), but exhibit selectivity, safety, and
mass-balance issues.[9] Recent work has shown that dilute HCl
acts as a lixiviant for the metals in printed-circuit boards,[6d]
but due to a lack of selectivity the commercial reagents are
likely to recover significant quantities of unwanted materials.