A novel electrode architecture for passive direct methanol fuel cells

The supply of cathode reactants in a passive direct methanol fuel cell (DMFC) relies on naturally breathing oxygen from ambient air. The successful operation of this type of passive fuel cell requires the overall mass transfer resistance of oxygen through the layered fuel cell structure to be minimized such that the voltage loss due to the oxygen concentration polarization can be reduced. In this work, we propose a new membrane electrode assembly (MEA), in which the conventional cathode gas diffusion layer (GDL) is eliminated while utilizing a porous metal structure for transporting oxygen and collecting current. We show theoretically that the new MEA enables a higher mass transfer rate of oxygen and thus better performance. The measured polarization and constant-current discharging behavior showed that the passive DMFC with the new MEA yielded better and much more stable performance than did the cell having the conventional MEA. The EIS spectrum analysis further demonstrated that the improved performance with the new MEA was attributed to the enhanced transport of oxygen as a result of the reduced mass transfer resistance in the fuel cell system.

[1]  Rong Chen,et al.  Mathematical modeling of a passive-feed DMFC with heat transfer effect , 2005 .

[2]  Toshiyuki Momma,et al.  Design and fabrication of pumpless small direct methanol fuel cells for portable applications , 2004 .

[3]  Qin Xin,et al.  Study of sintered stainless steel fiber felt as gas diffusion backing in air-breathing DMFC , 2004 .

[4]  Jaesung Han,et al.  Direct methanol fuel-cell combined with a small back-up battery , 2002 .

[5]  Rongzhong Jiang,et al.  Effect of operating conditions on energy efficiency for a small passive direct methanol fuel cell , 2006 .

[6]  Rong Chen,et al.  The effect of methanol concentration on the performance of a passive DMFC , 2005 .

[7]  M. Aulice Scibioh,et al.  On the consequences of methanol crossover in passive air-breathing direct methanol fuel cells , 2005 .

[8]  Jun Shen,et al.  Architecture for portable direct liquid fuel cells , 2006 .

[9]  T. Zhao,et al.  Synthesis and physical/electrochemical characterization of Pt/C nanocatalyst for polymer electrolyte fuel cells , 2004 .

[10]  Christopher K. Dyer Fuel cells for portable applications , 2002 .

[11]  Won-Yong Lee,et al.  Pore size effect of the DMFC catalyst supported on porous materials , 2003 .

[12]  In-Hwan Oh,et al.  Performance evaluation of passive DMFC single cells , 2006 .

[13]  Keith Scott,et al.  Engineering aspects of the direct methanol fuel cell system , 1999 .

[14]  T. Zhao,et al.  Effect of anode backing layer on the cell performance of a direct methanol fuel cell , 2006 .

[15]  Peter Urban,et al.  Impedance studies on direct methanol fuel cell anodes , 1999 .

[16]  Jenn-Jiang Hwang,et al.  Effect of breathing-hole size on the electrochemical species in a free-breathing cathode of a DMFC , 2006 .

[17]  Zhigang Qi,et al.  Open circuit voltage and methanol crossover in DMFCs , 2002 .

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

[19]  Shimshon Gottesfeld,et al.  Methanol transport through Nafion membranes : Electro-osmotic drag effects on potential step measurements , 2000 .

[20]  Peter Urban,et al.  Characterization of direct methanol fuel cells by ac impedance spectroscopy , 1998 .