A semi-continuous process of polymer enhanced ultrafiltration for removal of lead and cadmium has been elaborated. This operation mode would let a better coupling between industrial and laboratory-scale processes. Basically, it includes two stages: (1) metal retention, where we can obtain a permeate stream free of heavy metals; (2) polymer regeneration, where the polymer is regenerated in order to be reused in metal retention stage. In order to work in this way, a control system of permeate and feed stream flows has been installed in a batch laboratory-scale plant. In the first place, more suitable hydrodynamic operating parameters were obtained by ultrafiltration experiments. The influence of pH has been studied to fix the pH for metal retention and polymer regeneration experiments, and the operative polymer binding capacity has been determined to know the metal amount that can be treated. A mathematical model taking into account both conservation equations and competitive reactions which occur in the medium has been established. The development of this mathematical model (which is in good agreement with experimental data) enables to estimate design parameters to dimension pilot and industrial scale installations based on this process.