Analytical solutions of an isothermal two-dimensional model of a cathode flow channel in transport limited operational regimes of a proton exchange membrane fuel cell

被引:2
作者
Thosar, Aniket U. [1 ,2 ]
Lele, Ashish K. [1 ,2 ]
机构
[1] Acad Sci & Innovat Res AcSIR, CSIR Natl Chem Lab CSIR NCL Campus, Pune 411008, Maharashtra, India
[2] CSIR Natl Chem Lab, Pune 411008, Maharashtra, India
关键词
Proton exchange membrane fuel cells; Polarization curve; Transport resistance; Analytical modelling; OXYGEN REDUCTION KINETICS;
D O I
10.1016/j.ces.2018.10.048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the quest for obtaining accurate closed-form analytical expressions for polarization curve of a proton exchange membrane fuel cell (PEMFC), we have recently presented a two-dimensional model that accounts for oxygen concentration gradient and velocity gradient along the depth of a cathode flow channel. The model was developed for the case when Tafel kinetics of oxygen reduction reaction (ORR) on the cathode governs the overall rate of oxygen consumption. An improved match between predictions of the model and full three-dimensional simulations was obtained over the entire range of current density compared with earlier models which assumed homogenous oxygen concentration in the channel depth and plug flow velocity profile. In reality however, ORR kinetics is often not the rate limiting step for oxygen consumption in the cathode catalyst layer (CCL) at high current density since the Tafel kinetics is modulated by transport resistances in the CCL. In this article, we extend our two-dimensional analytical model to two different transport-limited regimes of CCL operation namely, slow oxygen transport across the CCL and slow proton transport across the CCL. We compare model predictions with results of full three-dimensional simulations in both cases and show that they are in excellent agreement even in these transport limited operational regimes of PEMFC. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:166 / 175
页数:10
相关论文
共 20 条
[1]   A Modified Agglomerate Model with Discrete Catalyst Particles for the PEM Fuel Cell Catalyst Layer [J].
Cetinbas, Firat C. ;
Advani, Suresh G. ;
Prasad, Ajay K. .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2013, 160 (08) :F750-F756
[2]   Investigation of Proton Transport in the Catalyst Layer of PEM Fuel Cells by Electrochemical Impedance Spectroscopy [J].
Cimenti, M. ;
Bessarabov, D. ;
Tam, M. ;
Stumper, J. .
ELECTRODE PROCESSES RELEVANT TO FUEL CELL TECHNOLOGY, 2010, 28 (23) :147-157
[3]   Resolving the Three-Dimensional Microstructure of Polymer Electrolyte Fuel Cell Electrodes using Nanometer-Scale X-ray Computed Tomography [J].
Epting, William K. ;
Gelb, Jeff ;
Litster, Shawn .
ADVANCED FUNCTIONAL MATERIALS, 2012, 22 (03) :555-560
[4]   A comparison of different approaches to modelling the PEMFC catalyst layer [J].
Harvey, D. ;
Pharoah, J. G. ;
Karan, K. .
JOURNAL OF POWER SOURCES, 2008, 179 (01) :209-219
[5]   A study of the agglomerate catalyst layer for the cathode side of a proton exchange membrane fuel cell: Modeling and optimization [J].
Khajeh-Hosseini-Dalasm, N. ;
Fesanghary, M. ;
Fushinobu, K. ;
Okazaki, K. .
ELECTROCHIMICA ACTA, 2012, 60 :55-65
[6]   How important is oxygen transport in agglomerates in a PEM fuel cell catalyst layer? [J].
Kulikovsky, A. A. .
ELECTROCHIMICA ACTA, 2014, 130 :826-829
[7]   Polarization curve of a PEM fuel cell with poor oxygen or proton transport in the cathode catalyst layer [J].
Kulikovsky, A. A. .
ELECTROCHEMISTRY COMMUNICATIONS, 2011, 13 (12) :1395-1399
[8]   The regimes of catalyst layer operation in a fuel cell [J].
Kulikovsky, A. A. .
ELECTROCHIMICA ACTA, 2010, 55 (22) :6391-6401
[9]   Performance of catalyst layers of polymer electrolyte fuel cells: exact solutions [J].
Kulikovsky, AA .
ELECTROCHEMISTRY COMMUNICATIONS, 2002, 4 (04) :318-323
[10]   On the origin of voltage oscillations of a polymer electrolyte fuel cell in galvanostatic regime [J].
Kulikovsky, AA ;
Scharmann, H ;
Wippermann, K .
ELECTROCHEMISTRY COMMUNICATIONS, 2004, 6 (07) :729-736