Page 98 - Introduction to Transfer Phenomena in PEM Fuel Cells
P. 98

Mass Transfer Phenomena     87
                             The convective forces that dominate  the mass transfer in the flow
                           channels are mainly imposed by the flow of fuel (hydrogen), while the flow
                           conditions of the oxidant can be controlled by the user. High reagent flow
                           rates can provide good distribution at the catalytic sites of the electrodes, but
                           this can also cause problems in the overall fuel cell and can even damage the
                           polymer  membrane. The diffusive forces  acting  on the surface of the
                           electrodes are supported  by convective forces upstream (from the flow
                           channels). Indeed, the velocity of the reagents decreases along its path to the
                           diffusion layers where diffusion begins. The consumption of gaseous
                           reactants and the production of water at the cathode are a function of the
                           flow of electrons passing through the external circuit, and therefore of the
                           intensity, through the electrochemical reactions. In other words, the material
                           flow densities are directly related to the current density delivered by the fuel
                           cell  [RAM 05]. The diagram in  Figure 3.2 shows  a general overview of
                           material flows. In what follows, we will consider the case of steady state and
                           unidirectional mass transfer (Ox) for a PEMFC.





















                                      Figure 3.2. The different material flows in a PEM fuel cell


                                                                      –2
                             The current  density (j) expressed in  [A.cm ] is related to the  molar
                           electron flow density, we then write:

                                       j
                                 N − =                                                    [3.1]
                                  e   F
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