Page 282 - Biofuels Refining and Performance
P. 282

Fuel Cells  261


             The polarization losses result in a further decrease in actual cell volt-
           age (V) from its ideal potential E (V   E   potential drop due to losses).
           The activation polarization loss is dominant at low current density. This
           is because electronic barriers have to be overcome prior to current and
           ion flows. Activation polarization is present when the rate of an electro-
           chemical reaction at an electrode surface is controlled by sluggish elec-
           trode kinetics. Therefore, activation polarization is directly related to the
           rates of electrochemical reactions. In an electrochemical reaction with
               > 50   100 mV, activation polarization is described by a semi-
           h act
           empirical equation known as the Tafel equation:
                                          RT       i
                                  h act   5  a  b ln a b
                                           nF      i 0

           where   is the electron transfer coefficient of the reaction at the elec-
           trode (anode or cathode), and i is the exchange current density. The Tafel
                                      0
           slope for the PEMFC electrochemical reaction is about 100 mV/decade
           at room temperature. Thus there is an incentive to develop electrocat-
           alysts that yield a lower Tafel slope [2, 3, 11, 12].
             Ohmic losses occur because of the resistance to the flow of ions in the
           electrolyte and resistance to the flow of electrons through the electrode
           materials. Decreasing the electrode separation and enhancing the ionic
           conductivity of the electrolyte can reduce the ohmic losses. Both the
           electrolyte and fuel cell electrodes obey Ohm’s law; the ohmic losses can
           be expressed by the equation: h ohm    iR, where i is the current flowing
           through the cell and R is the total cell resistance, which includes ionic,
           electronic, and contact resistance. See Figure 9.4.
             Due to the consumption of reactants at the electrode by an electro-
           chemical reaction, the surrounding material is unable to maintain the



              700
                                 Cathode loss
              600
             Polarization (mV)  400  Cathode loss (O )
              500
                                              2
              300

              200
                                      Electrolyte IR loss
              100
                                        Anode loss (H )
                                                  2
                 0     200    400    600      800
                                         2
                       Current density (mA/cm )
           Figure 9.4 Activation losses in a PEM fuel cell [1].
   277   278   279   280   281   282   283   284   285   286   287