Page 295 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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2 72  High Temperature Solid Oxide Fuel Cells: Fundnmentafs, Design and Applications

           of the cell design, component materials, and fabrication processes, performance
           stability  with  time,  and performance  variation  with  temperature.  Often  the
           results of  screening tests are reported  as power density (W/cm2) figures, and
           record values of maximum power density are extensively quoted. However, this
           measure  can  be  confusing  because  power  density  varies  greatly  with  fuel
           composition and with electrode polarisation. The i-V  curves for SOFCs are often
           linear and therefore allow an interpretation in terms of  area-specific resistance
           (ASR). Even  though  ASR  has  no  generally  accepted  definition, it  is  much
           less dependent on test conditions than power density, and it is preferable to use
           it  to  compare screening test  results.  The concept  of  ASR  is discussed in the
           next section.



           10.4 Area-Specific Resistance (ASR)

           A fuel cell stack can be regarded as a ‘black box’ into which hydrogen (gas) and
           oxygen (air) are inputs, and electricity and exhaust gases are outputs. For such a
           stack, ASR is defined as:
                     Emf  - U
               ASR =
                         i

           where Emf is the electromotive force with the inlet fuel and air, and U is the cell
           voltage at the current density, i, at the design point. A possible design point, for
           example, might be 0.6 V at 1000°C, a fuel utilisation of  85% and an air flow of 4
           times the stoichiometric amount (‘4 stoichs’).
             The cell voltage, U, should be measured independently of  the leads carrying
           the current, i.e. separate potential probes should be used. This ASR is in most
           cases not very sensitive to small variations in cell voltage and fuel utilisation. By
           determining the ASR  at a few different temperatures,  an apparent activation
           energy, EA, may be derived. Thus, in a voltage interval (from say 0.5 to 0.7 V)
           and  a  temperature  interval  (say  from  650  to  lOSOT), the  cell  may  be
           characterised,  with  fair  approximation, by  only two  characteristic  numbers,
           namely ASR at one temperature and EA.
             In case the i-V  curve is concave, it may be tempting to use a differential ASR
           (i.e. the tangent) at high current densities as this gives a nice low value. Such a
           number has the drawback that it does not reflect the cell performance over the
           full polarisation range as does the quantity defined by Eq. (1).
             Often, cell tests are conducted with very low fuel and air utilisations because
           these are easier to perform than the ‘realistic’ tests with high fuel utilisation. In
           case of insignificant fuel and oxygen utilisations, the relevant definition of ASR is
           again  that  of  Eq.  (l), but  the  insignificant  utilisation  makes  this  value
           incomparable  to  ASR  derived  from  experiments  with  high  fuel  utilisation,
           because  the  concentration  polarisation  resistance  due  to  the  fuel  and  air
           conversion can be a considerable fraction of  the total cell resistance. Thus, it is,
           in general, necessary to specify also the fuel and oxygen utilisation together with
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