Spent pickling acid
from the industrial galvanizing process currently
requires specialist disposal, yet there is the potential to recover
the zinc as a valuable metal. In this work, we compare the extraction
of zinc using tributyl phosphate from real galvanizing effluent and
laboratory prepared solutions. Both commercial and handmade hollow
fiber membrane contactors are used for this purpose. While the zinc
is effectively extracted, care must be taken to prefilter the solution
upstream of the membrane contactor to minimize crud formation and
interfacial effects. The extraction of both zinc and HCl from the
effluent is satisfactorily described using mathematical models for
both the multicomponent equilibria and mass transfer balances. In
development of the multicomponent equilibrium model, the thermodynamic
equilibrium constants obtained from the ZnCl2–NaCl–HCl
aqueous system were found to be applicable to the ZnCl2–FeCl2–HCl system.