Page 260 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
P. 260

Electrode Polarisations  2 3 7

                         0.020-  .  ,  .   ~  .  ,  .  ,  .  ,  .  ,  .  ,  .  ,   *  ,  .  ,  .
                                   20 wt% c
                                                                ,
                     h            -. 22.5 wt% C                ,
                     -         .........                      ,'
                      m
                     L  0.015-
                     .-            25 wt% C                ,.   ,'
                      c        -                          /'
                     .a-       .......  27.5 wt% C
                      a,
                     +             30 wt% C              I'
                                                       ,,'
                      0                               ,
                      e   0.01c-                     0-
                      !!                         .'
                                                    0'
                                                   ,'
                                                               ..-.
                     0                          0.          ,_..-
                                                         ,,...-.
                      W
                     u                    .'  0'  0'   _,._..-..-
                     2   0.005-          C'  .'   0.  0'   .-..
                      m                         _..-.   ..........  .........  .........
                                          _..-''
                                             _'.I"
                     0             *.  C'  C'  C'  ..-''  ..........  ...........   ..........
                                     .-..-
                                ,.  -..-.  ..........   ...............
                                 ,'
                              ,,;,..;:::;   .,.: ::., .....................
                         0.000,-;-"j'"'
          reformation and shift reactions, as n7ell as multi-component transport must be
          addressed.
            The presence of gaseous hydrogen in the fuel makes gaseous transport easier,
          thus lowering anode concentration  polarisation,  even when GO and GO2 are
          present. With pure hydrogen as the fueI, for an anode thickness on the order of
          --I  mm, with fresh fuel the i,,  can be as large as 5 A/cm2 at 800°C or even larger.
          This allows for the fabrication of relatively thick anode-supported cells, without
          unduly  increasing  concentration  polarisation.  This  is  one  of  the  principal
          advantages  of  an anode-supported  design  over  other  designs.  Greater  care,
          however, should be exercised when working with cathode-supported designs to
          ensure that cathodic concentration polarisation does not limit cell performance.
          9.4 Activation Polarisation

          Electrode reactions involve charge transfer as a fundamental  step, wherein a
          neutral species is converted into an ion, or an ion is converted into a neutral
          species. Both reactions thus involve electron transfer. At the cathode, the charge
          transfer reaction involves the conversion of  an oxygen molecule into oxide ions.
          The  electrodes  in  solid  state  electrochemical  devices  may  either  be  purely
          electronic conductors, or may exhibit both ionic and electronic conductivity (the
          so-called mixed ionic electronic conduction, MIEC). In addition, the electrodes
          may  be  either  single  phase  or  composite,  two-phase.  For  the  purposes  of
          illustration, in what follows we will examine the overall cathode reaction in a
          system with a single phase, purely eIectronically conducting electrode.
            The oxygen reduction  reaction  is  a multi-step process, usually comprising
          several parallel reaction pathways. A thorough understanding of the elementary
          processes in  SOPC  cathodes  under  realistic  operating  conditions has  eluded
          researchers because of  such multiplicity of  pathways. Thus, despite numerous
   255   256   257   258   259   260   261   262   263   264   265