This study describes and presents the results of a new electrochemical approach to co-production of hydrogen and electric power using a steam-carbon fuel cell, within which carbon-containing species are kept physically separate from the hydrogen stream by a solid oxide electrolyte membrane. The fuel cell used for this purpose consists of H 2 , H 2 O (g) /Pt/YSZ/Pt/C (s) ,CO,CO 2 and measurements are taken between 600 and 900 C. Peak electrical power generated at 900 C is 8 mW/cm 2 at a current density of 40.5 mA/ cm 2 corresponding to simultaneous production of carbon-free hydrogen at a rate of 354 g H 2 /m 2 day. Electrochemical behavior and cell loss mechanisms are studied using impedance spectroscopy in different cell arrangements operating in steam-carbon and air-carbon modes. Exchange current densities extracted from these measurements indicated activation energies of 80.3 6 7.9 kJ/ mol for oxygen reduction, 132 6 12 kJ/mol for CO oxidation, and 189 6 35 kJ/mol for steam reduction. These results indicate that steam reduction is the dominant loss mechanism with significant contribution from CO oxidation kinetics. Modeling results for the carbon bed indicate that a bed height of 7 mm is capable of supporting cell current densities of 700 mA/cm 2 at 85% effective char utilization, allowing for high performing steam-carbon fuel cells for the simultaneous production of hydrogen and electrical work. Hydrogen is a desirable fuel because it is both an effective energy carrier as well as a clean burning fuel with minimal impact on the environment. Unfortunately, hydrogen does not occur naturally, and must be generated from other sources. If widespread use of hydrogen is to be achieved, an efficient method for distributed hydrogen production is desired due to the cost and technical challenges posed by hydrogen transportation and storage.Currently, the majority of hydrogen production is performed centrally using steam reforming of methane, and to a lesser extent, coal. The fuel is reformed with steam and then undergoes the water-gas shift reaction to produce hydrogen. Unfortunately, this process produces a hydrogen stream that is contaminated by various carbonaceous species, and therefore requires expensive separation techniques to clean the gas. Carbon monoxide remnants in the hydrogen gas are of particular concern, as even trace amounts of CO in the hydrogen stream render the hydrogen product undesirable for catalytic processes due to CO poisoning. This is a critical problem especially for low temperature fuel cells. In addition, the reforming process is only economically feasible at large scales, requiring expensive storage and distribution of the hydrogen product to its point of use.A variety of alternative hydrogen production schemes that attempt to solve or avoid the limitations of reforming have been proposed. Thermal decomposition of steam into hydrogen and oxygen is one such option, but this reaction is thermodynamically uphill and energetically expensive. Another approach is the electrolysis of water in an e...