Page 336 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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3 12  High Temperature Solid Oxide Fuel Cclls: Fundamentals, Design and Applications

         generation calculated. In an approximate 3-D cell or stack model, it is customary
         to use a lumped electrochemical heat generation: that is, one assumes a uniform
         distribution of the reversible and irreversible heat generation over the respective
         electrode. Using a more advanced electrode-level model, the distribution of heat
         generation  in  the  electrodes  can  be  analysed, which  may  yield  important
         information for structural stability of the electrodes and their interfaces with the
         electrolyte and the current collector/gas channel profiles.
           The  heat  source  terms  discussed  above  are  used  in  the  energy  balance
         equations of the flow and thermal models for both cell and stack simulations. To
         manage the computation cost, most simulations avoid the full CFD treatment of
         the flow.  However, full  CFD  treatments  provide  more  accurate  and  detailed
         information on the flow in an SOFC system. With increased computing power,
         more and more full CFD simulations are expected to appear.
           Figure 11.5 shows sample cell modelling results: the steady-state temperature,
         current density,  and  species  concentration  distributions.  As  can  be  seen  by
         comparison with Figure 11.2, the steady-state temperature distribution is quite
         different from that during the rapid startup.
           Figure  11.6 shows the  steady-state  modelling  results  for  a  tubular  SOFC
         design, as reported by Ferguson et al. [29]. Clearly, the characteristic operating

















                                                         ) HI mass fraction












          (4 0: mass fraction    (e) PEN temperature    \.) HJQ massfraction

         Figure 11.5  Sample results for planar SOFC in cross-flow configuration: a, air temperature, max. 899"C,
         min. 625°C; b. current, A/cm2: max. = 1.46. min. = 0.300; c, H,  mass fraction. kglkg: max. 0.0385, min.
         0.00472  (CO distribution  similar); d,  02 mass  fraction.  kglkg:  max.  0.231, min.  0.182; e,  PEN
         temperature.  "C: max.  911, min.  643; f, H20 mass fraction,  kglkg:  max.  0.224. min.  0.0387 (CO,
                                     distribution similar ).
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