Operation-relevant modeling of an experimental proton exchange membrane fuel cell

Abstract A current–voltage ( I – V ) curve, also known as a polarization curve, is generally used to express the characteristics of a proton exchange membrane (PEM) fuel cell system. The behavior of a PEM fuel cell is highly nonlinear and it is important to incorporate process nonlinearity for control system design and process optimization. Therefore, it is essential to generate the I – V curve from the model as the operating condition changes. A first principle one-dimensional water and thermal management model is developed to generate the I – V curve. The model considers the effects of water transport across the membrane, activation overpotential, ohmic overpotential, concentration overpotential, pressure drops, and current density distribution along the channel of a PEM fuel cell. Design and modeling parameters are obtained via regression from four sets of experimental data. They are further validated as operating conditions (e.g., fuel cell temperature, anode pressure, cathode pressure, hydrogen stoichiometric ratio, air stoichiometric ratio, hydrogen humidification temperature, and air humidification temperature) change. A sensitivity analysis example is used to illustrate the usefulness of the predictive model.

[1]  S. Dutta,et al.  Three-dimensional numerical simulation of straight channel PEM fuel cells , 2000 .

[2]  D. Maillet,et al.  Modelling of heat, mass and charge transfer in a PEMFC single cell , 2005 .

[3]  G. G. Stokes "J." , 1890, The New Yale Book of Quotations.

[4]  T. Nguyen,et al.  Multicomponent transport in porous electrodes of proton exchange membrane fuel cells using the interdigitated gas distributors , 1999 .

[5]  Ralph E. White,et al.  A water and heat management model for proton-exchange-membrane fuel cells , 1993 .

[6]  Daniel R. Lewin,et al.  Model-based Control of Fuel Cells: (1) Regulatory Control , 2004 .

[7]  N. Djilali,et al.  Influence of heat transfer on gas and water transport in fuel cells , 2002 .

[8]  Chao-Yang Wang,et al.  Electron Transport in PEFCs , 2004 .

[9]  Ned Djilali,et al.  THREE-DIMENSIONAL COMPUTATIONAL ANALYSIS OF TRANSPORT PHENOMENA IN A PEM FUEL CELL , 2002 .

[10]  A. Parthasarathy,et al.  Temperature Dependence of the Electrode Kinetics of Oxygen Reduction at the Platinum/Nafion® Interface—A Microelectrode Investigation , 1992 .

[11]  T. Springer,et al.  Polymer Electrolyte Fuel Cell Model , 1991 .

[12]  Hyunchul Ju,et al.  A single-phase, non-isothermal model for PEM fuel cells , 2005 .

[13]  Mark W. Verbrugge,et al.  A Mathematical Model of the Solid‐Polymer‐Electrolyte Fuel Cell , 1992 .

[14]  T. Nguyen,et al.  An Along‐the‐Channel Model for Proton Exchange Membrane Fuel Cells , 1998 .

[15]  Nathan P. Siegel,et al.  A two-dimensional computational model of a PEMFC with liquid water transport , 2004 .

[16]  Chaoyang Wang,et al.  Three-dimensional analysis of transport and electrochemical reactions in polymer electrolyte fuel cells , 2004 .

[17]  Wei-Mon Yan,et al.  Analysis of thermal and water management with temperature-dependent diffusion effects in membrane of proton exchange membrane fuel cells , 2004 .

[18]  T. Fuller,et al.  Water and Thermal Management in Solid‐Polymer‐Electrolyte Fuel Cells , 1993 .