In acid pickling before electroplating, the effective acid concentration deteriorates while the dissolved metal concentration increases continuously. By introducing electrodialysis (ED) between this operation and the following rinsing baths, these disadvantages are largely rectified. Recovered acid is continuously returned to the pickling bath and the amount of waste is drastically reduced. Depleted solution is reused in rinsing baths. Moreover, ED can avoid metallic impurity build-up in the acid pickling bath. First manipulations conducted on our laboratory equipment failed. So, ion-exchange membranes (IEMs) were characterized by conductivity measurements and polarization curves. Afterwards, a new selection of IEMs was performed. Faradic yields were calculated for various commercial anion- and cation-exchange membranes (AEMs and CEMs) in a Hittorf cell and ED conditions were refined. The relation between the hydrodynamics of ED and the limiting current density was checked by new measurements based on a tracer method successfully applied to electrochemical cells by our laboratory.