A solid oxide fuel cell system integrated with a distillation column (SOFC-DIS) has been proposed in this article. The integrated SOFC system consists of a distillation column, an EtOH/H2O heater, an air heater, an anode preheater, a reformer, an SOFC stack and an afterburner. Bioethanol with 5 mol% ethanol was purified in a distillation column to obtain a desired concentration necessary for SOFC operation. The SOFC stack was operated under isothermal conditions. The heat generated from the stack and the afterburner was supplied to the reformer and three heaters. The net remaining heat from the SOFC system (Q(SOFC,Net)) was then provided to the reboiler of the distillation column. The effects of fuel utilization and operating voltage on the net energy (Q(Net)), Which equals Q(SOFC,Net) minus the distillation energy (Q(D)), were examined. It was found that the system could become more energy sufficient when operating at lower fuel utilization or lower voltage but at the expense of less electricity produced. Moreover, it was found that there were some operating conditions, which yielded Q(Net) of zero. At this point, the integrated system provides the maximum electrical power without requiring an additional heat source. The effects of ethanol concentration and ethanol recovery on the electrical performance at zero Q(Net) for different fuel utilizations were investigated. With the appropriate operating conditions (e.g. C-EtOH = 41 %, U-f = 80% and EtOH recovery = 80%), the overall electrical efficiency and power density are 33.3% (LHV) and 0.32 W cm(-2), respectively. (c) 2007 Elsevier B.V. All rights reserved.