Page 332 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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308  High Temperature Solid Oxide Fuel Cells: Fundamentals, Design and Applications


         11.5 Cell- and Stack-Level  Modelling
         The coupled continuum-level  electrochemical, flow, and thermal  models  are
         usually  discretised  in  a  finite  element  mesh  [23,24].  When  the  necessary
         material  properties,  geometrical  parameters,  operating  parameters,  and
         boundary  conditions  are  supplied, cell-  and  stack-level performance  can  be
         analysed. The combined models can determine the cell/stack voltage, the total
         current output, temperature distribution, species concentration, etc.
           An  important  outcome  of  the  combined  models  at  the  cell  level  is  the
         cell efficiency, and at the stack level, the stack efficiency as well. The electrical
         efficiency of a cell and of the stack is defined as
             E,I  = electrical power output/chemical energy input per unit time   (23)

         for the cell in question, and for the stack, respectively.
           The electrical efficiency therefore depends to some extent on the definition of
         the fuel energy input and on whether power for gas pumping and the like is
         subtracted from the generated power. &,I  may be expressed in terms of  current,
         voltage, etc., as follows:
             eel = VI/(AHdn/dt)                                           (244

         This can be considered the product of three additional fundamental efficiencies,
         namely the ideal or thermodynamic efficiency ( AG/AH}, the voltage efficiency
         {V/Eo},  and the fuel utilisation (Uf}:
             E,]  = VI/(AHdn/dt)  = {AG/AH}(V/Eo}(Uf}                     (24b)


         The fuel utilisation, Uf, is the ratio of the delivered current to the stoichiometric
         current equivalent to the fuel flow rate:

             uf = I/(2Fdn/dt)                                             (244

           The  ideal  efficiency  AG/AH  may  be  considered  a  measure  of  the
         thermodynamic reversibility of the reaction and depends only on the operating
         temperature and fuel used. It is typically between 80 and 100%. The voltage
         efficiency and fuel utilisation,  as well  as the electrical energy efficiency, are
         useful measures for the success of the cell and stack design.
           Another  important figure of  merit  predicted by  the combined model is the
         power density of  a cell, or of the stack as a whole. The power density of  a cell is
         usually defined on the basis of the cell or electrode area, that is

             Pce.l = I(current).V(cell voItage)/A(area)                   (254

           The power density of a stack is conveniently defined  on the basis of stack volume:

             Pstack  = I(current) .V(staclr voltage)/V(stack volume)      (297)
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