Page 189 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
P. 189

166  High Temperaturr Solid  Oxide Fuel Cells: Fundamentals, Design and Applications

        already mentioned  [ 301 through this distributed reforming over the anode [41]
        (Figure 6.12). However, it is now evident that such a direct oxidation process,
        without reforming, requires an innovation in anode materials, diverging from
        the established nickel-zirconia  option.

                                   CO+ H,O-    CO,+  H,
                CH,  + EH,O
                            \ I














        Figure  6.12  Schematic  of  distributed  processing  of  humidijed  methane  with  internally  generated
                                     reaction products.

          Spacil's alternative transition metals for the cermet, iron and cobalt, though
        less active for the pyrolysis of hydrocarbons, do not have the corrosion resistance
        of  nickel  in  a  high-steam  environment. Considering  silver  and copper, their
        oxides either decompose or melt  at temperatures below  the requirements for
        cermet  sintering:  neither  are the metals  refractory  (Ag m.p.  962°C: Cu  m.p.
        1083°C). However, in catalytic technology the advantages of copper composites
        with ceria are recognised [42]. Partial reduction of copper oxide when exposed to
        fuel  at  elevated  temperature,  and  the  resulting  redox  properties,  permit
        exchange of  oxygen between the lattice and the gas phase, with availability for
        surface reactions. A copper-ceria  composite anode [43,44] is a recent promising
        initiative. The difficulty of sintering a copper composite was avoided by forming a
        porous zirconia skeleton on a dense electrolyte substrate of the same material,
        then introduction of copper and cerium as their nitrate salts in solution, followed
        by drying and pyrolysis, similar to a procedure already demonstrated for anode
        and cathode catalysts  [45]. Co-insertion  of  the two cations is  possible  since
        copper does not form a solid solution in ceria so the two phases remain separate
        as  required  for  functionality  of  the  electrode.  In  Figure  6.13  the  reported
        performance  of  cells  using  this zirconia-supported  copper-ceria  composite  is
        presented. Obviously the power density with methane fuel is significantly lower
        than that with hydrogen, but the synergetic catalysis by ceria is evident from the
        negligible power density with copper alone in the zirconia matrix. Figure 6.14
        presents evidence of the stability of the composite anode, in contrast to a nickel
        cermet where the fuel cell operation is suppressed irreversibly within 30 min by
        the  carbon  accumulation.  The  ceria-copper  system  is  now  being  further
        investigated for the direct oxidation of higher hydrocarbons [43].
   184   185   186   187   188   189   190   191   192   193   194