Page 84 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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Thermodynamics  6 1

         provides  a  first  idea  of  the behaviour  of  real cells under changing operation
         conditions.  It  can  be  assumed  that  the  reaction  enthalpy  and  the reaction
         entropy depend only slightly on the temperature as a first assumption. Thus the
         free enthalpy of the reaction at a higher temperature can be approximated with
         the  values  of  the  reaction  enthalpy  and  the  reaction  entropy  at  standard
         conditions and it depends on the temperature linearly and yields the reversible
         cell voltage, Eqs.  (26) and (27). The values  of  the reversible  cell voltage are
         calculated for the standard state 0, at lOOO"C/l bar and for 25°C and 1000°C at
         0.1 and 10 bar. These linearised values of the free enthalpy and the reversible
         cell voltage at different thermodynamic states are written as A'G*  and V*.  The
         water is always assumed to be in the gaseous phase because a SOFC operates at
         high temperatures. The values can be found in Table 3.1 and Figure 3.3.
           Equations  (7)  and  (28)  indicate  that  the  volumes  of  the  products  of
         the oxidation reactions of hydrogen and carbon monoxide are smaller than the



         Table 3.1  The reversible oxidation of hydrogen, carbon monoxide and methane
         Fuel                          H2              co              CH4
         A'P in kJ/mol                 -241.82         - 2 8 2.9 9     -802.31
         A'S"  in J/(mol K)             -44.37          -86.41           -5.13
         ArGOin kJ/mol                 -228.59         -257.23         -800.68
         A'G*  at lOOO"C, 1 bar in kJ/mol   -185.33    -172.98         -795.68
         ne'                              2               2               8
         V) in V                          1.185           1.333           1.037
         V* at 1000°C. 1 bar in V         0.960           0.896           1.031
         In(K) at 0.1 bar                 1.1513          1.1513          0
         In(K) at 10 bar                 -1.1513         -1.1513          0
         Vat25"C.O.l  barinV              1.170           1.318           1.037
         V at 1000°C. 0.1 bar in V        0.897           0.833           1.03  1
         Vat25"C. 10barinV                1.199           1.348           1.037
         V at 1000°C. 10 bar in V         1.024           0.960           1.031


                          1.4  ,
                          1 3                ......  p =  10 bar
                                             - p=  1 bar
                          1 2
                       >
                        c 1,1
                       .-
                        %  I
                       +-  m
                       T5  03
                       >        H,   CH,  (all pressures)
                          0.8
                          0,7
                          0,6 7
                            300     600     900      1200    1500
                                     Cell temperature in K
         Figure 3.3  The reversiblecell voltageofdiferentfuels at diferent states (p.T) ofthe environment (linearised
                                 model andassumption ofidealgas).
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