Modeling the Effects of Gas Channel Flooding on the Voltage-Current Characteristics of PEM Fuel Cell

Author(s):  
K. H. Wong ◽  
K. H. Loo ◽  
Y. M. Lai ◽  
Siew-Chong Tan ◽  
Chi K. Tse

It has been reported recently that water flooding in the gas channel (GC) has significant effects on the voltage-current characteristics of a proton exchange membrane (PEM) fuel cell. However, the theoretical treatment of these effects on the fuel cell performance is still preliminary. A one-dimensional fuel cell model including the effects of two-phase flow in the GC is proposed to investigate the influences of inlet conditions on the water distribution in fuel cell and its performance by means of coupling the GC and membrane electrode assembly (MEA) modeling domains. The model predicts that the GC conditions, which are closely correlated to the inlet conditions, significantly affect the liquid water saturation level in the MEA. An increase in the inlet air pressure or humidification level leads to more severe water flooding, while an increase in the inlet air flow rate helps mitigating the water flooding. The simulated voltage-current characteristics under various inlet conditions are verified against experimental data and simulation results of a published computational fluids dynamics (CFD) model. They indicate that the relative humidity and stoichiometry of inlet air are crucial to the fuel cell performance, particularly at high current densities, due to their influences on the liquid water distribution in the fuel cell. The correlations between the inlet conditions and the fuel cell performance are addressed in the proposed model through a more accurate treatment of two-phase water transport in the cathodic MEA and GC. These are important for appropriate water management in fuel cells.

Author(s):  
Jinglin He ◽  
Song-Yul Choe ◽  
Chang-Ouk Hong

The flow in gas flow channels of an operating polymer electrolyte membrane (PEM) fuel cell has a two-phase characteristic that includes air, water vapor and liquid water and significantly affects the water flooding, pressure distribution along the channels, and subsequently the performance of the cell and system. Presence of liquid water in channels prevents transport of the reactants to the catalysts and increases the pressure difference between the inlet and outlet of channels, which leads to high parasitic power of pumps used in air and fuel supply systems. We propose a model that enables prediction of pressure drop and liquid water distribution along channels and analysis of water flooding in an operating fuel cell. The model was developed based on a gas-liquid two-phase separated flow that considers the variations of gas pressure, mass flow rate, relative humidity, viscosity, void fraction, and density along the channels on both sides. Effects of operating parameters that include stoichoimetric ratio, relative humidity, and inlet pressure on the pressure drop and water flooding along the channels were analyzed.


2005 ◽  
Vol 143 (1-2) ◽  
pp. 125-135 ◽  
Author(s):  
Hong Sun ◽  
Hongtan Liu ◽  
Lie-Jin Guo

Author(s):  
Yun Wang ◽  
Ken S. Chen

The objective of this study is to make an attempt at developing a sub-model that can account for the presence of liquid water in the cathode channel and couple it with other key phenomena occurring in a PEM fuel cell, including those in the anode side. The two-phase sub-model in cathode gas flow channels is based on the two-phase mixture formula. Numerical results from case studies are presented in comparison with those predicted by the single-phase channel flow sub-model. Our preliminary results indicate that liquid water accumulates along the flow channels and builds up quickly once it emerges. For the operating conditions and cell geometry chosen for the case study present in the present work, our results show that the liquid water in the channel only slightly affects the fuel cell performance. More extensive case studies are needed.


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