Mehrtash, MehdiMehrtash, MehdiMehrtash, MehdıEnergy Systems Engineering2024-07-052024-07-05202212227-971710.3390/pr100713152-s2.0-85133725547https://doi.org/10.3390/pr10071315https://hdl.handle.net/20.500.14411/1783MEHRTASH, MEHDI/0000-0001-8543-7006In this paper, a three-dimensional model of a high-temperature anion-exchange membrane fuel cell (HT-AEMFC) operating at 110 degrees C is presented. All major transport phenomena along with the electrochemical reactions that occur in the cell are modeled. Since the water is exclusively in the form of steam and there is no phase transition to deal with in the cell, the water management is greatly simplified. The cell performance under various current loads is evaluated, and the results are validated against the experimental data. The cell performance is examined across a range of operating conditions, including cell temperature, inlet flow rate, and inlet relative humidity (RH). The critical link between the local distributions of species and local current densities along the channels is identified. The distribution of reactants continuously drops in the gas flow direction along the flow channels, causing a non-uniform local current distribution that becomes more pronounced at high current loads, where the rate of water generation increases. The findings show that while a higher inlet flow rate enhances the cell performance, a lower flow rate causes it to drop because of reactant depletion in the anode. The sensitivity analysis reveals that the performance of an AEMFC is highly dependent on the humidity of the gas entering the cell. While high inlet RH on the cathode side enhances the cell performance, high inlet RH on the anode side deteriorates it.eninfo:eu-repo/semantics/openAccessHT-AEMFCfuel cells3D modelinghigh temperaturerelative humiditylocal current density distributionArticleQ2107WOS:000833149400001