Page 243 - High Temperature Solid Oxide Fuel Cells Fundamentals, Design and Applications
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220  High Temperature Solid Oxide Fuel Cells: Fundamentals, Design and Applications

         the tube to a thickness of  around 50 pm, and a nickel current collector wire is
         inserted and brought out from the fuel entry side of the tube. On the outside of the
         electrolyte tube, the lanthanum strontium manganite cathode layer, some 100
         pm thick, is deposited, fired, and a silver wire is wound around it to obtain the
         cathode current. Figure  8.25b shows a cross-section  of  the cell region  on the
         tube, illustrating the electrolyte support tube, the inner anode and nickel wire,
         and the outer cathode and its silver wire connector. Cell interconnection is made
         away from the cells in this design, so that a single interconnect material is not
         necessary: however, applying the anode and its current collector down inside a
         narrow tube is not trivial.
           Such a  design  of  microtubular SOFC  allows  small  SOFC  power  generation
         devices to be configured. For example, a microtubular SOFC can be heated in a
         burner to  provide  a  small  amount of  electrical  output to  drive  an electronic
         device.  One  such  arrangement  is  shown  in  Figure  8.26  with  a  long  YSZ
         electrolyte  tube  sealed  using  a  rubber  connector  to  a  gas  inlet  pipe,  and
         extending through the thermal insulation into a hot zone at 800°C [41-441.  In
         this case the long YSZ  support tube acts as an inlet pipe to bring fuel to the
         electroded cell region of  the tube. The electroded cell area of  the tube extends
         typically  for  30 mm  near  the tube exit, the anode and cathode wires  being
         brought  out  for  external  connection  to  the  electrical  load.  Upstream  of  the
         electroded  region,  a  catalyst  layer  can be  coated  onto the YSZ  tube for  fuel
         processing, whereas downstream, it is possible to apply a combustion catalyst to
         aid the reaction of the spent anode gas with the surrounding air. The advantages
         of  this  design  are  rapid  start-up,  ease  of  sealing,  and  integrability  into
         conventional flame systems. Drawbacks are the high in-plane resistance of the
         cells, the long current leads, and the difficulty of connecting and stacking many
         small cells together.


                     rubber seal  I       I                        /I



             =b                                                     hot exhaust
           fuel                                          ,A
           plus                                ectrolyte t  ' uoes   n
           air      cold Lone                     hot Lone
                    insulation
         Figure 8.26  Microtubular SOFC system showing the YSZ electrolyte tube sealed with a rubber connector,
                             with theelectrodedcell regionin the hot zone.


           This cell design illustrates several inherent features; the ease of  sealing to a
         rubber connector in  the cold zone, the high thermal  shock resistance  which
         allows the electrolyte tube to go through the thermal insulation into the hot
         zone, the feasibility for carrying out some fuel processing  upstream of  the cell
         region, and the ease of combustion at the exit of the tube. Typically, the gas feed
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