Page 268 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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Electrode Polarisations  245


          (02, N2  in the cathode: H2, HzO in the anode) transport through the porous
          interstices, which are contiguous, to or away from reaction sites. (2) In the case
          of  two  phase  MIEC  materials,  electrons  (or  holes)  transport  through  the
          electronically conducting (contiguous) phase, oxygen ions transport through
          the ionically conducting (contiguous) phase, and the charge transfer reaction
          occurs at or near a TPB. In single phase MIEC, both electrons (and/or holes) and
          oxygen ions transport through the single-phase MIEC, and the charge transfer5
          reaction occurs along the surface of  the porous MIEC. In this manner, whether
          the  electrode  is  two-phase  or  single-phase,  the  electrochemical  reaction  of
          charge  transfer  is  spread from the  electrolyte/electrode  interface  over  some
          distance into the electrode. (3) The region  over which this spreading occurs
          depends upon  the  microstructure  as well  as the transport  properties  of  the
          electrode. Usually, the finer the microstructure, the smaller is the region over
          which the reaction  zone is spread out.  (4) Very  close to the  electrolyte, the
          current  is  predominantly  ionic,  and  outside  the  critical  thickness  into
          the electrode, the current is predominantly electronic. Over the critical or the
          threshold  thickness,  the  current  varies  from ionic  (near the  electrolyte)  to
          electronic  (towards the current collector). Thus, the electrode should exhibit
          MIEC  characteristics  at  least  over  this  critical  or  the  threshold  distance.
          Typically, this critical thickness is on the order of  a few, to few tens of  microns.
          This  layer  has  been  variably  referred  to  as  the  electroactive  layer,  the
          electrocatalytic layer, or the interlayer. As  the microstructure  in this region
          must  be  he, which  enhances  the  rate  of  electrochemical  reaction  (lowers
          activation  polarisation), also unfortunately  impedes gas transport  (increases
          concentration polarisation) due to the Knudsen diffusion effects, as well as due
          possibly to  adsorption/desorption effects. The existence of  a critical thickness
          fortunately  implies  that  the  electrode  microstructure  need  not  be  fine
          throughout the electrode. Thus, the overall polarisation can be minimised by
          grading the electrode microstructure  such that near the electrolyte/electrode
          interface, the electrode has a fine microstructure and exhibits MIEC properties;
          and away from the interface, the electrode has a coarse microstructure with a
          large pore size, and exhibits essentially electronic conduction.
            While the general features of  several of  the models are similar, the particular
          analytical  expressions, wherever  available, vary  widely  depending upon the
          details of a given model. In what follows, some of the equations from the work of
          Tanner et a1 for composite cathodes are given to illustrate the role of  various
          parameters [2 71. In the low current density limit, over which the Butler-Volmer
          equation  can be  linearised,  the effective charge transfer  or  the  polarisation
          resistance (activation polarisation only) for cathode interlayer thickness greater
          than the critical thickness can be given by [22]






             In the case of a single phase MIEC, the reaction may be regarded as that of oxygen incorporation (or
          removal) rather than that of charge transfer.
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