Page 178 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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Anodes  155

         eliminating  microfissuring  which  contributes to  electrode  ageing  [ 71.  Nickel
         oxide of grain size around 1 pm is now used, while the zirconia component often
         contains a proportion of  coarse powder 2 5 pm or larger [ 111 to form the anode
         structural skeleton and inhibit the nickel aggregation, mixed with 0.5 pm fine
         powder  to  promote  sintering.  The  powder  mixtures  are  applied  to  form  the
         electrode layer on the YSZ electrolyte substrate, 150 pm or thicker, which also
         provides the structural rigidity of the cell.
           A similar development  strategy applies to the more recent anode-supported
         cells, now beginning to find favour for operation at 800°C or lower. This lower
         temperature relaxes materials specifications throughout the system, permitting
         the  use  of  lower  cost  metallic  structural  and  interconnect  components.
         Another  benefit  is  diminished  thermomechanical  stress  and  reaction  at
         these lower temperatures, significantly improving durability. On the other hand,
         lower power output is unacceptable, so for YSZ electrolyte, its higher resistivity
         at temperatures under 800°C must be compensated by reduction in its thickness
         to 10 pm. Recent cells therefore tend to use the anode, not just as a functional
         component, but also structurally as the load and stress-bearing support for a thin
         electrolyte. As will be later noted, this structural cermet, up to 1 mm thick, can
         serve not only as the site of  oxidation of  a reformate  composed principally  of
         hydrogen and carbon monoxide, but also for the preliminary hydrocarbon fuel
         processing reactions. At lower temperatures also, the thermal activation of the
         oxidation reactions is significantly diminished, implying increased polarisation
         and  giving  added  importance  to  considerations  of  electrocatalysis  at  the
         anode [12]. In this case graded  anode structures are often  advisable, with a
         high-porosity large-grain substrate bearing a finer-structured electrocatalytically
         active functional layer to contact with the electrolyte  [ 131. The micrograph in
         Figure 6.3 shows materials of an anode-supported cell [14].























         Figure  6.3  Micrograph  of  anode-supported  thin electrolyte cell  structure.  On either side  of  the dense
         electrolyte is afine-structured  ‘functional layer’for the electrocatalytic promotion of the electrode reactions.
         The  full thickness of  the cathode layer is imaged, but onlg a small section of  the anode substrate (bottom).
                        (Reproduced bycourtesyof the Research Centre, Jiilich (FZJ).)
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