Amirkabir University of Technology Amirkabir Journal of Mechanical Engineering 2008-6032 51 2 2019 06 22 Numerical Investigation of Water Management in the Cathode and Anode Sides of Proton Exchange Membrane Fuel Cell Numerical Investigation of Water Management in the Cathode and Anode Sides of Proton Exchange Membrane Fuel Cell 227 248 1026 10.22060/mej.2017.12457.5350 FA H. Khaleghi Department of Mechanical Engineering, Tarbiat Modares University, Tehran, Iran K. Mohammadzadeh Department of Mechanical Engineering, Tarbiat Modares University, Tehran, Iran Journal Article 2017 02 02 Water management in a proton exchange membrane fuel cell is numerically modeled by considering the 2D, non-isothermal steady flow assumptions. Governing equations are solved in all cell layers including cathode and anode electrodes by finite volume method using a single-region approach. The effect of gas cross-over through the membrane is studied on cell performance. This consideration, not only improves the general accuracy of modeling, but also makes it possible to model energy losses due to direct reaction of reactant gases. The effect of some key variables such as liquid water diffusivity, current density, membrane thickness, etc. on PEMFC conditions such as the amount of saturated liquid water, power density, cell temperature, cross-over efficiency and so on are examined. It was observed that the amount of saturated liquid water on the anode side is considerably important. This observation addresses needs for further investigation of liquid water behavior in the anode electrode. The amount of liquid water saturation in both the cathode and anode electrodes is increased with increasing the current density. The results showed that at the current density of 0.2 A/cm2, cross-over effect causes about 10% reduction in cell efficiency and by decreasing the current density this effect is enhanced. Water management in a proton exchange membrane fuel cell is numerically modeled by considering the 2D, non-isothermal steady flow assumptions. Governing equations are solved in all cell layers including cathode and anode electrodes by finite volume method using a single-region approach. The effect of gas cross-over through the membrane is studied on cell performance. This consideration, not only improves the general accuracy of modeling, but also makes it possible to model energy losses due to direct reaction of reactant gases. The effect of some key variables such as liquid water diffusivity, current density, membrane thickness, etc. on PEMFC conditions such as the amount of saturated liquid water, power density, cell temperature, cross-over efficiency and so on are examined. It was observed that the amount of saturated liquid water on the anode side is considerably important. This observation addresses needs for further investigation of liquid water behavior in the anode electrode. The amount of liquid water saturation in both the cathode and anode electrodes is increased with increasing the current density. The results showed that at the current density of 0.2 A/cm2, cross-over effect causes about 10% reduction in cell efficiency and by decreasing the current density this effect is enhanced. https://mej.aut.ac.ir/article_1026_24146db4eb48c718b84cae0a0799dcfc.pdf