An isothermal, steady-state model of an anode in a direct methanol feed, po
lymer electrolyte fuel cell is presented. The anode is considered to be a p
orous electrode consisting of an electronically conducting catalyst structu
re that is thinly coated with an ion-selective polymer electrolyte. The por
es are filled with a feed solution of 2 M methanol in water. Four species a
re transported in the anode: water, methanol, hydrogen ions, and carbon dio
xide. All four species are allowed to transport in the x-direction through
the depth of the electrode. Species movement in the pseudo y-direction is t
aken into account for water, methanol, and carbon dioxide by use of an effe
ctive mass-transfer coefficient. Butler-Volmer kinetics are observed for th
e methanol oxidation reaction. Predictions of the model have been fitted wi
th kinetic parameters from experimental data, and a sensitivity analysis wa
s performed to identify critical parameters affecting the anode's performan
ce. Kinetic limitations are a dominant factor in the performance of the sys
tem. At higher currents, the polymer electrolyte's conductivity and the ano
de's thickness were also found to be important parameters to the prediction
of a polymer electrolyte membrane fuel cell anode's behavior in the methan
ol oxidation region 0.5-0.6 V vs, a reversible hydrogen electrode. (C) 1999
The Electrochemical Society. S0013-4651(97)12-114-0. All rights reserved.