Theoretical Model for the Optimal Design of Air Cooling Systems of Polymer Electrolyte Fuel Cells. Application to a High‐Temperature PEMFC

The cooling system of a high-temperature PEM fuel cell with a nominal electric power of 1.5 kW for a combined heat and power unit (CHP) has been designed using a thermochemical model. The 1D model has been developed as a simple, predictive, and useful tool to evaluate, design, and optimize cooling systems of PEM fuel cells. As proved, it can also be used to analyze the influence of different operational and design parameters, such as the number and geometry of the channels, or the air flow rate, on the overall performance of the stack. To validate the model, predicted results have been compared with experimental measurements performed in a commercial 2 kW air-forced open-cathode stack. The model has then been applied to calculate the air flow required by the designed prototype stack as a function of the power output, as well as to analyze the influence of the cooling channels configuration (cross-section geometry and number) on the heat management. Results have been used to select the optimum air-fan cooling system, which is based on compact axial fans.

[1]  Phatiphat Thounthong,et al.  Behaviour of a PEMFC supplying a low voltage static converter , 2006 .

[2]  J. García,et al.  Comparison of water management between two bipolar plate flow-field geometries in proton exchange membrane fuel cells at low-density current range , 2009 .

[3]  Song-Yul Choe,et al.  A high dynamic PEM fuel cell model with temperature effects , 2005 .

[4]  Natarajan Rajalakshmi,et al.  Thermal and electrical energy management in a PEMFC stack – An analytical approach , 2008 .

[5]  I. Hsing,et al.  Absorption, Desorption, and Transport of Water in Polymer Electrolyte Membranes for Fuel Cells , 2005 .

[6]  Dejan Brkić Comments on “Experimental study of the pressure drop in the cathode side of air-forced open-cathode proton exchange membrane fuel cells” by Barreras et al., Int. J. Hydrogen Energy, 36 (13) 2011, 7612–7620 , 2012 .

[7]  Félix Barreras,et al.  Experimental study of the pressure drop in the cathode side of air-forced Open-cathode proton exchange membrane fuel cells , 2011 .

[8]  Félix Barreras,et al.  Influence of CrN-coating thickness on the corrosion resistance behaviour of aluminium-based bipolar plates , 2011 .

[9]  Mohammad S. Alam,et al.  A dynamic model for a stand-alone PEM fuel cell power plant for residential applications , 2004 .

[10]  Félix Barreras,et al.  Cr and Zr/Cr nitride CAE-PVD coated aluminum bipolar plates for polymer electrolyte membrane fuel cells , 2010 .

[11]  C. Chamberlin,et al.  Modeling of Proton Exchange Membrane Fuel Cell Performance with an Empirical Equation , 1995 .

[12]  Datong Song,et al.  Transient analysis for the cathode gas diffusion layer of PEM fuel cells , 2006 .

[13]  Félix Barreras,et al.  Fluid dynamics performance of different bipolar plates: Part II. Flow through the diffusion layer , 2008 .

[14]  Junxiao Wu,et al.  Study of the effects of various parameters on the transient current density at polymer electrolyte membrane fuel cell start-up , 2009 .

[15]  K. Agbossou,et al.  Transient air cooling thermal modeling of a PEM fuel cell , 2008 .

[16]  Félix Barreras,et al.  Design and development of the cooling system of a 2 kW nominal power open-cathode polymer electrolyte fuel cell stack , 2012 .

[17]  Marcelo Godoy Simões,et al.  Simulation of fuel-cell stacks using a computer-controlled power rectifier with the purposes of actual high-power injection applications , 2003 .

[18]  Félix Barreras,et al.  Fluid dynamics performance of different bipolar plates , 2008 .

[19]  G. Eigenberger,et al.  Transport parameters for the modelling of water transport in ionomer membranes for PEM-fuel cells , 2004 .