In this work, the experimental procedure and mathematical model formerly developed was used to describe the electrodialytic (ED) recovery of trisodium citrate. By performing several voltage-current, electro-osmosis and desalination tests, the main engineering parameters (i.e., the ion transport numbers in solution and membranes, effective solute and water transport numbers, effective surface area and resistances of membranes, and limiting electric current) of the ED process under study were assessed. As expected, the electric resistance of the cationic membranes (R-c) resulted to be about constant (0.11 +/- 0.02 Omega) and independent of solute concentration, while that of the anionic ones (R-a) was not only greater than R-c, but also dependent on both the current applied and solute concentration. Moreover, in the ohmic region of the current-voltage curves R-a appeared to be a logarithmic function of the solution electric conductivity in the dilute compartment. On condition that the current applied was less than 2/3 of the limiting current for the cationic membrane (I-lim,I-c) the time course of the voltage applied to the ED stack when operating at a constant current of 0.75 or 1.5 A was adequately predicted with a mean percentage error of similar to 20%. (c) 2013 Elsevier B.V. All rights reserved.