We studied the operation of a twin-cell electrochemical filter for removing carbon monoxide (CO) from reformate hydrogen by periodically adsorbing and then electrochemically oxidizing CO on the electrode. During the adsorption step, we studied the effects of feed CO concentration, flow rate, electrode catalyst loading, type of feeder gas, and temperature on CO breakthrough. We then applied a fixed bed adsorber model to show that the breakthrough time could be accurately correlated to the adsorption-step operating parameters. Since the oxidation step was found to be much faster than that for CO breakthrough, adsorption time should dictate switching time. This insight was used to predict steady-state filter performance, and the prediction was validated for an electrochemical filter operated with CO contaminated hydrogen to decrease the CO concentration from 10,000 to 10 ppm. The model was also used to explore the employability of an electrochemical filter over a range of operating conditions by considering the comparative electrode area of a filter with that of a fuel cell. Proton exchange membrane fuel cells (PEMFC) efficiently convert chemical energy in hydrogen (H 2 ) to electrical energy. However, the low volumetric energy density of H 2 makes the fuel storage and transport cumbersome. Alternatively, H 2 can be generated at the point-ofuse from hydrocarbons via catalytic steam reforming.1 The reformate gas has carbon monoxide (CO) concentrations as high as 10,000 ppm, 2 whereas the platinum (Pt) anode, typically used in PEMFC, is susceptible to poisoning at concentrations as low as 10 ppm.3-4 In water-gas shift catalysis, typically used for removing CO from H 2 , improving the selectivity of oxidation of CO over H 2 faces thermodynamic limitations below a CO concentration of 1,000 ppm.5 Mitigation strategies such as operating fuel cells at elevated temperatures, 6 air-bleeding, [7][8] anode alloying 9-11 and in situ potential pulsing 4,12-13 have been explored to minimize the impact of CO poisoning. But the tolerance level of PEMFC has been improved only to a CO concentration of 100 ppm. 9,[14][15][16][17][18][19][20] In general, CO contamination in H 2 is handled by employment of CO removal techniques such as pressure swing adsorption (PSA), [21][22] or membrane separation, 23 or conversion of CO into methane in catalytic methanation [24][25][26] or carbon dioxide (CO 2 ) in preferential oxidation (PrOx) with air bleed. [7][8]14,[27][28][29][30][31][32][33][34][35][36][37][38][39] However, the consequent increase in cost due to fuel loss, 7 power loss, 40 components and space requirements 41 hampers the utilization of aforementioned techniques for commercially viable systems, especially in portable power applications. Balasubramanian et al. proposed an electrochemical filtering technique in which CO in reformate is concentrated by preferentially adsorbing on an electrocatalyst bed. Instead of purging as done in PSA, the adsorbed CO is electrochemically oxidized to CO 2 .42 Also, the ambient-pressure operation...