Page 221 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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198  High Tenrprr~turr Solid Oxide Fwl Cells: Fundamentals,  Design and Applications




                                                                   FUEL
              I NTE RC ON N E CT
                   ANODE
              ELECTROLYTE
                   CATHODE




                                  OXIDANT

                                Figure 8. I  Planar SOFC design.

        components  of  a planar SOFC. Advances in ceramic technology,  especially  in
        synthesising  fine  powders,  engineering  material  compositions,  tailoring
        composition/property/microstructure  relationships, and fabricating/processing
        intricate structures, have contributed to the increased interest in planar SOFCs
        since  early  1980s.  Significant  progress  has  now  been  made  on  the
        demonstration of fabricability, performance, and operation of planar SOFCs.
          A planar SOFC, like any other cell configuration,  must be designed to have
        the desired  electrical  and  electrochemical  performance,  along  with required
        thermal management and mechanical/structural  integrity  to meet  operating
        requirements  of  specified  power  generation  applications  [3].  The  key
        requirements  are discussed  below:  this  discussion  is  qualitative because  the
        specific requirements depend on selected designs and intended applications.

          6)   Electrical  performance.  This requirement means that the design  must
               minimise  ohmic  losses  in  the  stack.  Thus,  the  current  path  in  the
               components (especially those having low electrical conductivity) must be
               designed to be as short as possible. There must be good electrical contact
               and  sufficient  contact  area  between  the  components.  The  current
               collector must also be designed to facilitate current distribution and flow
               in the stack.
          (ii)  Electrochemical  performance. This requirement means that the design
               must  provide  for  full  open  circuit  voltages  and  minimal  polarisation
               losses. Thus, any significant gas leakage or cross-leakage and electrical
               short must be avoided. Fuel and oxidant must be distributed uniformly
               not only across the area of each cell but also to each cell of the stack. The
               gases must be  able to quickly reach the reaction sites to  reduce mass
               transport limitation.
          (iii)  Thermal management.  This requirement means that  the design  must
               provide  means  for  stack  cooling  and  more  uniform  temperature
               distribution  during  operation.  The  design  must  permit  the  highest
               possible temperature gradient across the stack.
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