Publication | Closed Access
Mathematical Modeling of Liquid-Feed Direct Methanol Fuel Cells
333
Citations
39
References
2003
Year
EngineeringMethanol CrossoverEnergy ConversionMethanolFuture FuelFuel ScienceFlow CellBiofuel CellChemical EngineeringProton-exchange MembraneTransport PhenomenaMethanol ConcentrationElectrical EngineeringMathematical ModelingMethanol CrossingElectrochemical CellMultiphase FlowElectrochemistryFuel Cells
The study delineates transport phenomena and electrochemical kinetics in liquid‑feed DMFCs and investigates how methanol feed concentration affects cell performance. A comprehensive CFD‑based model incorporates anode and cathode reactions, gas and liquid diffusion and convection in backing layers and flow channels, and the mixed‑potential effect of methanol crossover at the cathode. The model, validated against experiments, shows that higher methanol concentrations reduce voltage due to crossover, increase mass‑transport limiting current below 1 M, and at concentrations above 2 M limit performance by oxygen depletion, while the anode outlet void fraction reaches 95 % at 0.45 A cm⁻². © 2003 The Electrochemical Society; all rights reserved.
A two-phase, multicomponent model has been developed for liquid-feed direct methanol fuel cells (DMFC). In addition to the anode and cathode electrochemical reactions, the model considers diffusion and convection of both gas and liquid phases in the backing layers and flow channels. In particular, the model fully accounts for the mixed potential effect of methanol oxidation at the cathode as a result of methanol crossover caused by diffusion, convection, and electro-osmosis. This comprehensive model is solved numerically using computational fluid dynamics. The transport phenomena and electrochemical kinetics in a liquid-feed DMFC are delineated and the effects of the methanol feed concentration on cell performance are explored. The model is validated against DMFC experimental data with reasonable agreement. The void fraction at the anode outlet is found to be as high as 95% at a cell current density of 0.45 A/cm2 for a 7 cm long channel. Increase in methanol feed concentration leads to a slight decrease in cell voltage and a proportional increase in the mass-transport limiting current density for a methanol concentration below 1 M. However, when the methanol feed concentration is larger than 2 M, the cell voltage is greatly reduced by excessive methanol crossover and the maximum current density begins to be limited by the oxygen supply at the cathode. The oxygen depletion results from excessive parasitic oxygen consumption by methanol crossing over. © 2003 The Electrochemical Society. All rights reserved.
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