Page 162 - Introduction to Transfer Phenomena in PEM Fuel Cells
P. 162

The equations for interfacial temperatures are summarized in Table 4.4.
                                 Interfaces                 Temperature Heat Transfer Phenomena     151
                                    =
                                   x0                           T
                                                                 C
                                                   T +
                                    =
                                  xL       T GDL,C  = ( C  ( ( R GDL  R BP ) T⋅  BP,C )) ( ( R GDL  R BP ) ) 1+
                                      1
                                                       T +
                                   =
                                  xL            T BP,C  =  ( C  ( air  ⋅  R ⋅ T air  )) ( ( h air  ⋅  R 2 ) ) 1+
                                                           h
                                                                 2
                                      2
                                                       T +
                                                                  ⋅
                                   =
                                                            h
                                  xL            T BP,A  = ( C  ( air  ⋅ R T air  )) ( ( h air  ⋅  R 1 ) ) 1+
                                                                 1
                                      3
                                   =
                                  xL            T GDL,A  =  ( air  ⋅ R BP  ⋅ ( BP,A  −  T air )) T+  BP,A
                                                         h
                                                                  T
                                      4
                                                              ⋅
                                   =
                                  xL          T =  ( ( R GDL  R BP  ) ( GDL,A  − T BP,A )) T+  GDL,A
                                                               T
                                               A
                                      5
                                   =
                                                     T +
                                  xL            T = ( C   ( ( R m  R A ) T⋅  A  )) ( ( R m  R A ) ) 1+
                                                 m
                                      6
                                   =
                                  xL                            T
                                      7
                                                                 C
                                          Table 4.4. Summary of interfacial temperatures
                             Equations that give the temperature profile for each cell element are
                           shown in Table 4.5.
                                      Distances        Temperature  distribution
                                       0 →  L     Tx        ( GDL,C  −  T c  ) e GDL ) x⋅      +  T
                                                   () ( T=
                                                                                c
                                           1
                                      L →  L    Tx       ( BP,C  −  T GDL,C ) e BP ) x⋅      +  T GDL,C
                                                 () ( T=
                                       1
                                            2
                                      L →  L         Tx        ( m  −  T c ) e m ) x  ⋅    +  T
                                                      () ( T=
                                                                             c
                                            6
                                       7
                                      L →  L        Tx =      ( A  T M  ) e A ) x  ⋅    +  T
                                                      () ( T −
                                            5
                                                                             m
                                       6
                                      L →  L      Tx       ( GDL,A  − T A  ) e GDL ) x⋅      +  T
                                                   () ( T=
                                                                                A
                                            4
                                       5
                                      L →  L    Tx       ( BP,A  −  T GDL,A  ) e BP ) x⋅      +  T GDL,A
                                                 () ( T=
                                            3
                                       4
                                 Table 4.5. Summary of the equations giving the temperature profiles
   157   158   159   160   161   162   163   164   165   166   167