Page 327 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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Cell, Stack and System Modelling  303

            As discussed above, the I-V  relation of  a PEN element depends on material
          properties and electrode structures as well as on operating parameters such as
           gas  composition,  pressure,  and  temperature.  Using  a  simple  first-order
          electrochemical  model  and  the  potential  balance,  Eq.  (7), combined  with
           simplified  expressions  for  the  various  polarisation  contributions  such  as
           Eqs. (ga), (lob), and (11)-(14b), I-V  curves can be predicted. These predicted
           curves may be used to fit experimental I-V  data and deduce, from an optimal fit,
           certain material and structure properties such as Ri and i,a,  which cannot be
           measured  directly.  In cells with  sizable electrode  area, which  tend  to  have
           appreciable fuel and oxidant utilisation, temperature and gas partial pressures
           are local quantities dependent on the extent of the electrochemical and chemical
           conversion (i.e., the fuel and oxidant utilisations). The electrochemical model
          predicting  the  I-V  curve  simultaneously  yields  the  current  distribution,
           temperature distribution. and other quantities of interest.
             Figure 11.3 shows the theoretical and experimental I-V  relations of  a small-
           size  cell  (considered  isothermal)  for  different  fuel  compositions  at  a  set  of
           temperatures [ 141. The material properties were obtained by fitting the theory to
          the experimental data for 9 7% Hz + 3% HzO fuel. As shown, the simplified theory
           can predict variation in the I-V  curve with fuel composition reasonably well.
             To obtain accurate information about microstructural characteristics of SOFC
           electrodes, a set of experimental i-q  curves for a given electrode may be fitted,
           similar to Figure 11.3, against predictions of  a more complex porous electrode
          model, as discussed in Section 11.8.

                1.1
                1  .o                      electrochemical
                                                               sccm air flow rate
                                                             200 sccm fuel flow rat
                0.9
              >
               d0.8
               m
              -
              I
               0
              -
              2 0.7
               01
              u
                0.6
                0.5
                0.4
                  0.0   0.2   0.4   0.6   0.8   1.0   1.2   1.4   1.6   1.8   2.0
                                     Current Density, Nan2
                          Figure 7 1.3.  Predicfedand measlcredcellI-Vcurvesf143.


           1’8.4 Chemical Reactions and Rate Equations

           Wheo fuel cells are operating, the heat generation rate (the source term needed
           in the thermal-fluid model) depends on the rates of  the various chemical and
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