Numerical analyses of non-isothermal self-start behaviors of PEM fuel cells from subfreezing startup temperatures

In this paper, a multiphase multidimensional PEM fuel cell model for cold-start simulations has been employed for numerical analyses of the non-isothermal self-start behaviors of a PEM fuel cell from subfreezing startup temperatures, focusing on the coupled phenomena of the ice formation and temperature increase inside the cell. The roles played by many key influential parameters, including the water vapor concentration in the cathode gas channel, the initial water content inside the membrane, the operating current density, and the startup cell temperature, are carefully examined. Numerical results indicate that decreasing the interfacial water vapor concentration at the gas diffusion layer and gas channel surface on the cathode side of the cell would delay ice precipitation and prolong the cell operation time. Decreasing the operation current density and the initial water content inside the membrane, and increasing the startup cell temperature are beneficial for the non-isothermal cold starts of the PEM fuel cell and could lead to successful self-starts.

[1]  In-Hwan Oh,et al.  Characteristics of the PEMFC Repetitively Brought to Temperatures below 0°C , 2003 .

[2]  R. M. Moore,et al.  Polymer electrolyte fuel cell stack thermal model to evaluate sub-freezing startup , 2005 .

[3]  Manish Khandelwal,et al.  One-dimensional thermal model of cold-start in a polymer electrolyte fuel cell stack , 2007 .

[4]  Hua Meng,et al.  A PEM fuel cell model for cold-start simulations , 2008 .

[5]  Shanhai Ge,et al.  Characteristics of subzero startup and water/ice formation on the catalyst layer in a polymer electrolyte fuel cell , 2007 .

[6]  H. Meng A three-dimensional mixed-domain PEM fuel cell model with fully-coupled transport phenomena , 2007 .

[7]  Yun Wang,et al.  Analysis of the Key Parameters in the Cold Start of Polymer Electrolyte Fuel Cells , 2007 .

[8]  Chao-Yang Wang,et al.  Effects of operating and design parameters on PEFC cold start , 2007 .

[9]  Hua Meng,et al.  Numerical studies of cold-start phenomenon in PEM fuel cells , 2008 .

[10]  Hua Meng,et al.  A three-dimensional PEM fuel cell model with consistent treatment of water transport in MEA , 2006 .

[11]  Mario Zedda,et al.  Statistic analysis of operational influences on the cold start behaviour of PEM fuel cells , 2005 .

[12]  Shanhai Ge,et al.  In Situ Imaging of Liquid Water and Ice Formation in an Operating PEFC during Cold Start , 2006 .

[13]  Hubert A. Gasteiger,et al.  Oxygen Reduction Reaction Kinetics in Subfreezing PEM Fuel Cells , 2007 .

[14]  Masahiro Shiozawa,et al.  Super-cooled water behavior inside polymer electrolyte fuel cell cross-section below freezing temperature , 2008 .

[15]  Chao-Yang Wang,et al.  Non-isothermal cold start of polymer electrolyte fuel cells , 2007 .

[16]  Christopher Hebling,et al.  Start Up and Freezing Processes in PEM Fuel Cells , 2007 .

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

[18]  J. Jorné,et al.  Investigation of Low-Temperature Proton Transport in Nafion Using Direct Current Conductivity and Differential Scanning Calorimetry , 2006 .

[19]  Chao-Yang Wang,et al.  Transient analysis of polymer electrolyte fuel cells , 2005 .

[20]  Chao-Yang Wang,et al.  Analysis of Cold Start in Polymer Electrolyte Fuel Cells , 2007 .

[21]  Kazuhiko Yoshida,et al.  Behavior of water below the freezing point in PEFCs , 2007 .

[22]  Chao-Yang Wang,et al.  A Multiphase Model for Cold Start of Polymer Electrolyte Fuel Cells , 2007 .

[23]  Hua Meng,et al.  A two-phase non-isothermal mixed-domain PEM fuel cell model and its application to two-dimensional simulations , 2007 .

[24]  In-Hwan Oh,et al.  Effects of Water Removal on the Performance Degradation of PEMFCs Repetitively Brought to < 0 ° C , 2004 .

[25]  Xianguo Li,et al.  Non-isothermal transient modeling of water transport in PEM fuel cells , 2007 .

[26]  J. Jorné,et al.  PEM Fuel Cell Operation at − 20 ° C . I. Electrode and Membrane Water (Charge) Storage , 2008 .

[27]  H. Meng Numerical investigation of transient responses of a PEM fuel cell using a two-phase non-isothermal mixed-domain model , 2007 .

[28]  Rajesh K. Ahluwalia,et al.  Rapid self-start of polymer electrolyte fuel cell stacks from subfreezing temperatures , 2006 .

[29]  R. Mcdonald,et al.  Effects of Deep Temperature Cycling on Nafion® 112 Membranes and Membrane Electrode Assemblies , 2004 .

[30]  Chao-Yang Wang,et al.  Isothermal Cold Start of Polymer Electrolyte Fuel Cells , 2007 .