Reversible performance loss induced by sequential failed cold start of PEM fuel cells

This study correlates the post start cell performance and impedance with the cold start process in the subzero environment. The sequential failed cold starts are deliberately conducted as well as the start at small current density. Here the failed cold start means the cell voltage drops to or below zero within very short time during the start process. It is found that there are reversible performance losses for the sequential failed cold starts, while not obvious degradation and no recovery happen for the start at small current density. Using the thin film and agglomerate model, it is confirmed that this is due to the water blocking effect. Comparing the results from different start processes, a model with respect to the shifting of reactive region within the catalyst layer is applied to explain that the reversible performance loss is associated with the amount of the generated water or ice and the water location or distribution during cold start. The relationship of the cold start performance at high current density and the pore volume in the catalyst layer is also discussed.

[1]  B. Yi,et al.  Kinetic investigation of oxygen reduction reaction in sub-freezing acid media , 2008 .

[2]  B. Yi,et al.  Electrochemical impedance investigation of proton exchange membrane fuel cells experienced subzero temperature , 2007 .

[3]  B. Yi,et al.  Conductivity of aromatic-based proton exchange membranes at subzero temperatures , 2008 .

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

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

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

[7]  Dietmar Gerteisen,et al.  Degradation effects in polymer electrolyte membrane fuel cell stacks by sub-zero operation : An in situ and ex situ analysis , 2008 .

[8]  Shanhai Ge,et al.  Cyclic Voltammetry Study of Ice Formation in the PEFC Catalyst Layer during Cold Start , 2007 .

[9]  Shengsheng Zhang,et al.  Effects of freeze/thaw cycles and gas purging method on polymer electrolyte membrane fuel cells , 2006 .

[10]  B. Yi,et al.  Comparative Study of PEM Fuel Cell Storage at − 20 ° C after Gas Purging , 2007 .

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

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

[13]  I. Raistrick Impedance studies of porous electrodes , 1990 .

[14]  Wei Liu,et al.  Degradation behaviors of polymer electrolyte membrane fuel cell under freeze/thaw cycles , 2010 .

[15]  Tomohiro Ogawa,et al.  The Design and Performance of a PEFC at a Temperature Below Freezing , 2004 .

[16]  U. Stimming,et al.  Conductance of Nafion 117 membranes as a function of temperature and water content , 1995 .

[17]  Zhongjun Hou,et al.  Catalytic hydrogen/oxygen reaction assisted the proton exchange membrane fuel cell (PEMFC) startup at subzero temperature , 2008 .

[18]  M. Mench,et al.  1D Transient Model for Frost Heave in Polymer Electrolyte Fuel Cells II. Parametric Study , 2007 .

[19]  Hongwei Wang,et al.  Analysis of PEMFC freeze degradation at −20 °C after gas purging , 2006 .

[20]  Stefano Ubertini,et al.  First Steps Towards Fuel Cells Testing Harmonisation: Procedures and Parameters for Single Cell Performance Evaluation , 2003 .

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

[22]  T. E. Springer,et al.  Electrical Impedance of a Pore Wall for the Flooded‐Agglomerate Model of Porous Gas‐Diffusion Electrodes , 1989 .

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

[24]  Yun Wang,et al.  Analysis of Reaction Rates in the Cathode Electrode of Polymer Electrolyte Fuel Cell I. Single-Layer Electrodes , 2008 .

[25]  Hongwei Wang,et al.  Effects of reverse voltage and subzero startup on the membrane electrode assembly of a PEMFC , 2007 .

[26]  Bryan S. Pivovar,et al.  Freeze/Thaw Effects in PEM Fuel Cells , 2006 .

[27]  Chao-Yang Wang,et al.  Water removal from a PEFC during gas purge , 2008 .

[28]  Matthew M. Mench,et al.  Physical degradation of membrane electrode assemblies undergoing freeze/thaw cycling: Micro-structure effects , 2007 .

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

[30]  B. Yi,et al.  Sub-freezing endurance of PEM fuel cells with different catalyst-coated membranes , 2009 .

[31]  Mariana Ciureanu and,et al.  Electrochemical Impedance Study of PEM Fuel Cells. Experimental Diagnostics and Modeling of Air Cathodes , 2001 .

[32]  Zhigang Shao,et al.  Investigation of resided water effects on PEM fuel cell after cold start , 2007 .

[33]  Y. Bultel,et al.  Catalyst gradient for cathode active layer of proton exchange membrane fuel cell , 2000 .

[34]  Sébastien Rosini,et al.  Experimental and theoretical investigations on a proton exchange membrane fuel cell starting up at subzero temperatures , 2009 .

[35]  Matthew M. Mench,et al.  Physical degradation of membrane electrode assemblies undergoing freeze/thaw cycling: Diffusion media effects , 2008 .

[36]  Dieter Brüggemann,et al.  Experimental investigation of parameters influencing the freeze start ability of a fuel cell system , 2009 .

[37]  Rodney L. Borup,et al.  Cold start of polymer electrolyte fuel cells: Three-stage startup characterization , 2010 .

[38]  B. Yi,et al.  Ionic resistance of the catalyst layer after the PEM fuel cell suffered freeze , 2008 .

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