Page 54 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
P. 54

History  35

           the  ‘excluded volume model’ [8 71.  Doubts concerning the rapid  intermixing
           of  the  different cations  of  oxide electrolytes and oxide electrode layers were
          resolved by in~~estigations with radionuclides [88-901, which confirmed the low
          mobility of the cations in mixed oxides with fluorite structure. (In CaO-stabilised
          zirconia the ratio of the self-diffusion coefficients of  the anions to that of  the
          cations is larger than lo6 even at 1700°C).
            At high oxygen pressures, oxide phases show defect electron (hole) conduction
           (oxidation  semiconduction)  and  at  low  oxygen  pressures  excess  electron
           conduction  (reduction  semiconduction).  The  transport  number  of  excess
          electrons in Zro.s$ao.lsOl.s3  as a function of the oxygen partial pressure could
          be  determined  by  measurements  with  a  Ca,CaO/air  cell  [79].  The  hole
          conduction of zirconia-based solid electrolytes was noticed for the first time when
          cells  with  Ni,NiO  reference  electrodes  for  gas  potentiometry  [44,91  J  were
          tested in air. The harmful oxygen permeability was measured potentiometrically
          in 1965 1921.
            Also  in  1965, the  fundamentals  of  gas  potentiometry  were  presented,
          including the range of free oxygen and of oxygen in equilibria, and the ‘neutral’
          transition  range  [93].  Calculations  and  measurements  in  the  case  of
          potentiometric titrations of different gases were in good agreement in all three
          ranges [94]. (The sudden change of the cell voltage of a hydrogen/air cell zt the
          equivalence point  when  oxygen  was  fed to  the  hydrogen  had  already been
          shown  graphically by  Archer  et al.  [59].) Thus the investigations  started  for
          SOFCs led to the development of  oxygen sensors (lambda probes) now widely
          used  in  automobiles.  (A  zirconia  cell  working  potentiometrically  was  first
          proposed by Loos in 1969 as a sensor for O2 and CO for the regulation of the air/
          fuel ratio in cars [ 9 51 .)
            Another  less  well-known  by-product  of  SOFC  development  was  the
          electrochemical thermometry: i.e. the determination of elevated temperatures on
          thethermodynamicscalewithC0,C02,H2,H20 11961 orOz concentrationcells [97].
            The first investigations of polarisation phenomena in solid oxide fuel cells were
          conducted by the research groups in Sverdlovsk [61,98], Frankfurt [63], Geneva
          11691, GrenobIe [70] and Nagoya [71]. In the detailed investigations of  fuel cells
          with cerium-lanthanum  mixed oxides by Takahashi et al. [71] the polarisations
          observed were much smaller at the anode than at the cathode because by partial
          reduction of  the solid electrolyte, a mixed conductor (solid solution of  Ce203 in
          CeOz) was  formed  at  the  anode  giving  a  depolarising  interlayer.  Detailed
          investigations of  the polarisation of  solid electrolyte cells by  determining the
          complex admittance were first conducted by Bauerle in 19 69 [99].
            The high conductivity of cerium-lanthanum mixed oxides and the favourable
          polarisability of  electrodes on such solid electrolytes was  already  stimulating
          application ideas in the 1960s. But electronic conductivity of  these electrolytes
          above 600°C was seen as a weighty problem [71]. The influence of  electronic
          conductivity  on  the  cell performance was  investigated  first  by  means  of  an
          equivalent  circuit  [40,100].  The  results,  shown  in  Figure  2.8,  led  to  the
          conclusion that the ion transport number has to be greater than 0.9  if  a solid
          electrolyte was to be successful in a SOFC [loo].
   49   50   51   52   53   54   55   56   57   58   59