The present study shows upon, electrochemical removal of Ca 2+ and Mg 2+ ions from aqueous solutions. Calcite and brucite precipitation occurs through a chemical process following the electrochemical generation of OH − ions in the vicinity of the electrode surface. The kinetics of the electrochemical calcite and brucite precipitation were examined by measuring the electric conductivity as a function of time using different voltages and concentrations. The electric current density initially augments the electrochemical precipitation of calcite, but at a sufficiently higher current density the precipitation rate tends to an asymptotic limit. Furthermore, the precipitation rate of calcite is limited by diffusion kinetics of HCO 3 − ions and does not vary with the Ca 2+ concentration. In contrast, the electrochemical precipitation of brucite correlates with current density, as there are no limitations in diffusion kinetics. With increasing Mg 2+ concentration the rate constant of brucite decreases as small Mg 2+ concentrations or high pH values promote the generation of MgOH + (aq.) species in the reaction zone, which are responsible for an enhanced precipitation rate. In addition the specific energy consumption required for 1 mmol/L Ca 2+ removal strongly increases with the applied voltage, whereas the energy consumption required for 1 mmol/L Mg 2+ removal is nearly independent of the applied voltage.