Page 35 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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16  High Temperature Solid Oxide Fuel Cells: Fundamentals, Design and Applications

         anode but requires ceria or other catalysts to provide suitable sites for direct
         oxidation [ 3 61.
           Fuel reforming can also take place on nickel at the anode. This occurs when
         steam is added to the hydrocarbon fuel, typicalIy at a ratio of  3 parts steam to
          1 part of fuel. The reaction of methane is then given by
             CH4 + HzO  +.  CO + 3H2


           The hydrogen and carbon monoxide released by this reaction can then react
         individually  with  oxide  ions  emerging  from  the  electrolyte.  Usually  the  CO
          conversion is sluggish so the shift reaction also occurs on the anode to produce
         more hydrogen:

              CO+HzO  + COz  +H2

            It was demonstrated in the 1960s that hydrocarbons could be injected directly
          into SOFCs if  steam was supplied [37]. The steam can beneficially be obtained
          from the spent fuel stream. The main problem with direct use of hydrocarbons is
          that coke can form to block up and contaminate  the  anode.  There  are two
          damaging reactions which can occur on the nickel:
              2co  +. coz + c

              CH4  + 2H2 + C

            When  carbon  formation  was  investigated  in  detail,  by  temperature-
          programmed reaction, three different types of  material were discovered on the
          nickel, as indicated by the temperature  required for oxidation [38]. The most
          stable carbon could not be  removed beIow  1100 I< and tended to form when
          current was flowing through the cell.
            The other damaging mechanism of  SOFC failure stems from fuel impurities.
          Sulphur is the most prevalent impurity and can be present  up to  l?h level in
          marine diesel fuel. SOFCs cannot operate with this  amount of  sulphur. More
          typically, natural  gas often has ‘odorant’ sulphur compounds added to make
          leaks  more  easily detectable.  Even  the  lower levels  of  such  additions, about
          10 ppm, are damaging for SOFCnickel anodes, and the upper limits around 100 ppm
          could cause failure  in  about  1 h  of  operation. There are two  approaches to
          solving this problem: adding a sulphur absorber to the fuel processing unit: and
          using anode metals which are less affected by sulphur. Fortunately, the levels of
          sulphur in gasoline and diesel fuel are now being reduced for environmental
          reasons, with the best formulations containing less than 10 ppm.
            The second difficulty is the number of  additives in conventional fuels which
          have  been  formulated for  other  technologies.  For  example, regular  gasoline
          contains  more  than  100 different molecules,  some  added  as  lubricants  or
          surfactants. Moreover, the mixture can change with time and place because the
          standard is dictated by octane number and not composition. Consequently, it is
          unlikely that SOFCs will be able to run directly on gasoline, although this has
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