A one-dimensional non-isothermal model of a proton exchange membrane (PBM)
fuel cell has been developed to investigate the effect of, various design a
nd operating conditions on the cell performance, thermal response and water
management, and to understand the underlying mechanism. The model includes
variable membrane hydration, ternary gas mixtures for both reactant stream
s, phase change of water in the electrodes with unsaturated reactant gas st
reams, and the energy equation for the temperature distribution across the
cell. It is found that temperature distribution within the PEM fuel cell is
affected by water phase change in the electrodes, especially for unsaturat
ed reactant streams. Larger peak temperatures occur within the cell at lowe
r cell operating temperatures and for partially humidifed reactants as a re
sult of increased membrane resistance arising from reduced membrane hydrati
on. The non-uniform temperature rise can be significant for fuel cell stack
s. Operation on reformed fuels results in a decrease in cell performance la
rgely due to reduced membrane hydration, which is also responsible for redu
ced performance at high current densities for high cell operating pressures
. Model predictions compare well with known experimental results. (C) 2001
Elsevier Science B.V. All rights reserved.