Page 155 - Introduction to Transfer Phenomena in PEM Fuel Cells
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144     Introduction to Transfer Phenomena in PEM Fuel Cells
                             The sorption phenomena  thus reflect the equilibrium between a liquid
                           phase (adsorbed) and a gaseous phase (desorbed) at an interface. Transfers
                           are therefore subject to a phase change at this interface.
                             Several authors have focused on measuring the enthalpy of water sorption
                           in a Nafion® polymer  membrane.  Watari  et al. [WAT 03]  reviewed the
                           values used in the literature and reported values varying between 42 and
                                   −1
                           52 kJ.mol   according to the water content of the membrane or its
                           pretreatment. However, there was no clear  correlation between measured
                           values and experimental conditions. More recently, Burnett et al. [BUR 06]
                           took measurements using Nafion®112 and obtained values between 43 and
                                   −1
                           60 kJ.mol .
                             It is not currently possible to know the exact sorption enthalpy as a
                           function of the operating conditions. However, the measured values are close
                           to the latent heat of water vaporization L vap (Atkins and De Paula [ATK 02]
                                               −1
                           give L vap = 41.6 kJ.mol  to 353 K). In what follows, the sorption enthalpy of
                           water in the  membrane  will be considered equal to the latent heat of
                           vaporization of the water L vap [ROS 99].

                             According to Ramousse et al. [RAM 09], the algebraic character of the
                           calculated water flows makes it possible to treat sorption and desorption in
                                                                                –2
                           the same way. The heat flow densities are expressed in [W.m ]:
                                 
                                 Q sorp  =Δ H sorp  ⋅  N a H O                           [4.37]
                                  a
                                          HO
                                                  2
                                            2
                           and:
                                 
                                 Q sorp  =−Δ H sorp  ⋅ N c H O                           [4.38]
                                  c
                                            HO
                                                   2
                                             2
                             In order for the production of water in liquid form at the cathode to be
                           generated, we write:
                                                j
                                 N c HO  =  N a HO  +  2F                                [4.39]
                                    2
                                           2
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