Lead is a highly toxic heavy metal, found in water and air, which should be treated. Lead removal from wastewater is an important problem in battery industries. The separation process by means of electrodialysis (ED) shows several advantages such as highly selective desalination, high water recovery, only a partial addition of chemicals and the possibility of a stop-and-go operation. The performance of an ED plant is determined by a set of fixed and variable process parameters such as stack construction, feed and product concentrations, membrane permselectivity, flow velocities, current density, recovery rates, etc. For an efficient operation of ED, the process has to be optimized in terms of overall costs considering component design and properties as well as all operating parameters. Effects of now rate, temperature and voltage at different concentrations using two types of commercial membranes on lead removal were studied. Experiments were carried out on three levels of concentration: 100, 500 and 1000 ppm; temperature: 25, 40 and 60degreesC; voltage: 10, 20 and 30 V; flow rate: 0.07, 0.7 and 1.2 mL/s using a laboratory ED cell. The results show that increasing voltage and temperature improved cell performance; however, the separation percentage decreased with an increasing flow rate. At concentrations of more than 500 ppm, dependence of separation percentage on concentration diminished. Using membranes with higher ion-exchange capacity resulted in better cell performance.