Page 257 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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234  High Temperature Solid Oxide Fuel Cells: Fundamentals, Design and Applications

          simplified equivalent circuit can be used to describe the process, using what is
          known as the Warburg element, which consists of  a number  of  resistors and
          capacitors [5]. The presence of capacitors ensures that the response time or time
          constant is non-zero. Since the relevant time dependences are not describable by
          simple first order kinetics, it is not appropriate to describe response time as a time
          constant. Nevertheless, a characteristic time can be defined, which depends on
          electrode thickness, electrode microstructure and the representative diffusivity.
            In  terms  of  physically  measurable  parameters,  analytical  expressions  for
          anodic concentration polarisation  have been  derived which  allow its explicit
          determination as a function of  a number of  parameters. One of  the important
          parameters is the anode-limiting current density, which is the current density at
          which the partial pressure of the fuel, e.g. H2, at the anode/electrolyte interface,
          is near zero such that the cell is starved of fuel. If this condition is realised during
          operation,  the  voltage  precipitously  drops  to  near  zero.  This  anode-limiting
          current density,  i,,,  has the following form [6]






          where  D,(,J)  is the effective gaseous  diffusivity through  the  anode, and  I,  is
          the  anode  thickness.  The  effective  anode  diffusivity  contains  the  binary
          diffusivity of  the relevant  species, namely Hz  and H20, DH*-H,o,  the  volume
          fraction of  porosity, VVca), and the tortuosity factor, t, [3,4]. If the fuel contains
          hydrocarbons, multi-component nature of  gaseous diffusion must be addressed.
          The tortuosity factor is a measure of  the tortuous nature of the anode through
          which  diffusion must  occur. In very fine microstructures,  the tortuosity  as a
          phenomenological parameter may include effects of Knudsen diffusion, surface
          diffusion,  and  possible  effects  of  adsorption/desorption.  The  anodic
          concentration polarisation is then of the form [6]


                                                                            (10)


            Note  that  as  the  current  density  approaches  the  anode  limiting  current
                                                                       -
          density, that is when i --f ias, the first term approaches infinity. The maximum
          value of  q:onc is limited by  the OCV.  Thus, the maximum  achievable current
          density will always be less than ias. The dependence of the anodic concentration
          polarisation given by equation (10) on various parameters can be qualitatively
          described  as  follows:  From  the  standpoint  of  physical  dimensions,  and
          microstructural parameters, the lower the volume fraction porosity, the higher
          the tortuosity factor, and the greater the anode thickness, the higher is q;onc.
          From the standpoint of fuel gas composition, the lower the partial pressure of
          hydrogen,  p&,  the  higher  is  the  q:onc.  The  temperature  dependence  is
          complicated. It is seen that  i,,  cx T1l2, since D,(,J)  cx T3/2, which would mean $one
          increases as temperature  decreases. At the same time, as seen from equation
          (10). Y $ ~ ~ ~linearly  dependent  on  temperature,  which  would  mean  q:onc
                    is
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