Page 57 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
P. 57

The focal point  of work  on solid oxide fuel cells during  this period  was  the
           development  of  electrode materials. An  early  problem was  poor  adhesion of
           the anode layers, which became obvious in 1963 [59]. Spacil as early as 1964
           found the now well-known solution of using layers of nickel closely mixed with
           solid electrolyte material [loll.
             It was considerably more difficult to find a suitable cathode material. It turned
           out  to  be  a  misconception  to  think  that  small concentrations  of  polyvalent
           cations  in  mixed  oxides  with  fluorite  structure  produce  a  high  electronic
           conductivity. Layers with a high concentration of praseodymium at the cathode
           and high concentration of cerium at the anode had to be realised in order to
           achieve anything near the desired conductivities [102]. Only mixed oxides with
           uranium proved to be a good material for stable layers with eIectronic and ionic
           conductivity,  spreading  the  electrode  reactions  across  the  three  phase
           boundaries of  electrode/electrolyte/gas.  This idea was confirmed by the result
           that thin mixed conducting interlayers between  the pure electrolyte and the
           metallic  conductor  considerably  reduced  polarisation  phenomena  [lo31 and
           led  to  high  current  densities  [104].  An  optimised material  with  polyvalent
           uranium ions in mixed oxides with fluorite structure suitable for sintering on
           sohid  oxide  electrolytes  without  phase  boundaries  was  developed  by
           Tannenberger in  1967 [lO5, 1061; it proved to be a favourable interlayer in
           cathodes and anodes [ 10 7,lO 81.
             Indium oxide with different additives was proposed as a cathode material in
           1966 [lo91 and frequently used (e.g. [110, 107, 1081). However, electronically
           conducting  perovskites  soon  began  to  dominate  the  developments for  both
           cathode and interconnect. The use of Lal-xSrxCo03 for the air electrode of  solid
           oxide  fuel  celIs  marked  the  beginning  [lll],  followed  in  1967  by
           recommendations of PrCoOs [112] and of mixtures of the oxides of Pr, Cr, Ni and
           Co [ 11 31. Strontium-doped lanthanum chromite, even now the most important
           ceramic interconnection material, was proposed by Meadowcroft in 1969 [114].
           For cathodes, the situation in 1969 was summarised [ 11 51 as: 'It is apparent that
           a fully satisfactory air electrode for high temperature  zirconia electrolyte fuel
           cells is still lacking.'
             The  SOFC  stacks  developed  in  1963  were  not  safe  enough  for  power
           generation  aboard  spacecrafts. SOFCs  for  electrolysis  of  the  atmosphere  in
           manned spacecrafts (recovery of oxygen from COz and H2O in stacks of bell-and-
           spigot  cells,  carbon  deposition,  and  hydrogen  separation  [116])  were  also
           investigated. For this application, electrolyte discs (6.3 cm diameter, 1.4-1.6
           mrn  thick) and for the first time mixed oxides of  Zr  and Sc [117] were used.
           Flat-plate designs of SOFCs had been proposed earlier (Figure 2.9 [118,119]).
             Terrestrial applications aimed at an economic SOFC system for the production
           of  electrical power from coal and air at an overall efficiency of  60% or greater.
           With a conceptual  100 kW coal-burning fuel cell power system (Figure 2.10
           [l20]), coal could be gasified using the heat and combustion products emerging
           from the fuel cell stacks.
             In  1968 General Electric took  up the idea  of  electrochemical  dissociation
           of  water vapour in solid oxide cells [121-1231.  They hoped to produce cheap,
   52   53   54   55   56   57   58   59   60   61   62