Page 164 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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Cathodes  141

             It  is  well  known  that  oxidation/  corrosion  of  metallic  materials  is
           enhanced [63] in the presence of  water vapour. Chromium poisoning can also
          be enhanced in the presence of water vapour. The vapour pressure of chromium
          containing species increases with increasing water vapour pressure, because
           Cr02(0H)2 is relatively stable species in the presence of  water vapour [64]. Its
          vapour pressure shows only a small temperature dependence so that even at
           low  temperatures  its  vapour  pressure  is  high.  Taniguchi  et  aI. found  that
           the  degradation  increases  with  water  vapour  pressure  consistent  with  the
           increasing vapour pressure of Cr-containing species.
             Chromium  poisoning  was  found  to  depend  strongly  on  the  particular
           combination  of  electrolyte  and  cathode  by  Matsuzaki  et  al.  [65].  In  their
           investigations, the most severe degradation occurred in LSM/YSZ combination,
           whereas no apparent degradation occurred in LSCF/SDC (samaria-doped ceria)
           combination as seen in Figure 5.14. These results appear to be consistent with
          Taniguchi’s  results  [ 5 91.  As  described  previously,  the  cathode  reaction
           mechanism is quite different in the LSM  and the LSCF  cathodes.  In LSM, the
           oxide  ion  diffusivity  is  low  and  only  the  three-phase  boundaries  are  the
          electrochemically active sites. The oxygen potential gradient appears near these
          sites. This gives rise to the driving force for chromium-containing species to attack
          the  electrochemically  active  sites  resulting  in  the  deposition  of  chromia-
           containing oxides that are responsible for performance degradation. On the other
          hand, in LSCF, the rate-determining step is the surface reaction rate. Thus, the
           electrochemically active sites are widely distributed on the surfaces of the LSCF
           cathode.  The  oxygen potential  difference corresponding  to  the  overpotential
           appears on the surface, leading to no driving force for chromium-containing
           species to attack any electrochemically active sites. Matsuzaki et al.  [65] also
           observed that degradation is different between the LSM/YSZ and the LSM/SDC
           combinations.  Although it is difficult to ascertain the proper reasons for this
           difference, a possible explanation can be derived from the differences in water






                             -500                  LSCF/SDC












                                0         50         100       150
                                             time I ks
                 Figure 5.24  Chromiumpoisoningfor different electrode/electrolyte combinations 1651.
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