A model is presented for the reduction of hexavalent chromium in a parallel-plate electrochemical reactor via a homogenous reaction between Cr͑VI͒ and Fe͑II͒ generated at the iron anode. The effects of the space velocity of the feed solution, the concentration of supporting electrolyte, the distance between the electrodes, and the cell potential on conversion of Cr͑VI͒ to Cr͑III͒, are discussed. This study indicates that for reduction of Cr͑VI͒ using Fe͑II͒, the space velocity must be maintained below 0.02 s −1 or the system becomes limited by the rate of reduction of Cr͑VI͒ by Fe͑II͒. Increasing the current density by increasing the cell potential, increasing the amount of supporting electrolyte, and decreasing the distance between the electrodes increases single pass conversion of Cr͑VI͒ to Cr͑III͒; however, increasing the current density also increases the specific energy required by the system.