Enhancement of PEM fuel cell performance by flow channel indentation

被引:135
作者
Ghanbarian, A. [1 ]
Kermani, M. J. [2 ,3 ]
机构
[1] Amirkabir Univ Technol, Dept Aerosp Eng, 424 Hafez Ave, Tehran 158754413, Iran
[2] Amirkabir Univ Technol, Dept Mech Eng, 424 Hafez Ave, Tehran 158754413, Iran
[3] Ctr Solar Energy & Hydrogen Res ZSW, D-89081 Ulm, Germany
基金
美国国家科学基金会;
关键词
CFD; Channel partial blockage (indentation); Fuel cells; Performance enhancements; Parametric study; CONVECTIVE HEAT-TRANSFER; SINGLE-PHASE; MATHEMATICAL-MODEL; FIELD; EXCHANGE; 2-PHASE; TRANSPORT; PRINCIPLE; TRANSIENT; CATHODE;
D O I
10.1016/j.enconman.2015.12.036
中图分类号
O414.1 [热力学];
学科分类号
摘要
A three-dimensional, steady, single-phase flow of oxygen, nitrogen and water vapor mixture in the cathode of proton exchange membrane (PEM) fuel cell was numerically studied here. It was shown that the performance of the cell was enhanced by partial blockage of the flow channels in a parallel flow field. Since, channel indentation could increase oxygen content within the catalyst layer. It was observed that the influence of channel indentation in high current density regions was noticeable. Various types of blocks with profile shapes: square (SOJ, semicircle (SC) and trapezoid (TR) were considered. Enhancements were compared with the no-dent (ND) called as the base case. The voltage to current relation was modeled using the Tafel equation. This provided the distribution of current density at a prescribed cell voltage. The computations were performed at 333 K, 100,000 Pa, water dew point temperature 313 K, and 50% utilization within the range of 0.2-0.8 V. It was predicted that the flow turns to be two-phase in high current density regions (say cell voltages less than 0.4 V). To push the condensate out of the flow field, adequate pressure gradient were required. This prerequisite was already taken into account in this study. A parametric study considering the influences of dent heights and arrangements, exchange current density, fluid viscous resistance and rib sizes were considered providing enhancements over 25% in the net power. The present study gives a very helpful guideline for flow field manufactures. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:356 / 366
页数:11
相关论文
共 43 条
[1]   Modeling optimizes PEM fuel cell performance using three-dimensional multi-phase computational fluid dynamics model [J].
Al-Baghdadi, Maher A. R. Sadiq ;
Al-Janabi, Haroun A. K. Shahad .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (12) :3102-3119
[2]   A two-dimensional, transient, compressible isothermal and two-phase model for the air-side electrode of PEM fuel cells [J].
Baboh, M. Khakbaz ;
Kermani, M. J. .
ELECTROCHIMICA ACTA, 2008, 53 (26) :7644-7654
[3]   A MATHEMATICAL-MODEL OF THE SOLID-POLYMER-ELECTROLYTE FUEL-CELL [J].
BERNARDI, DM ;
VERBRUGGE, MW .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1992, 139 (09) :2477-2491
[4]   Gas flow field with obstacles for PEM fuel cells at different operating conditions [J].
Bilgili, Muhittin ;
Bosomoiu, Magdalena ;
Tsotridis, Georgios .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (05) :2303-2311
[5]  
CAUX S, 2010, J ENERGY CONVERS MAN, V51, P320, DOI DOI 10.1016/J.ENCONMAN.2009.09.028
[6]   The effects of channel depth on the performance of miniature proton exchange membrane fuel cells with serpentine-type flow fields [J].
Chang, Dyi-Huey ;
Wu, Shin-Yi .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (35) :11659-11667
[7]  
Choghadi HR, 2011, 10 INT C SUST EN TEC
[8]   Proton exchange membrane fuel cells performance enhancement using bipolar channel indentation [J].
Dehsara, Mohammad ;
Kermani, Mohammad J. .
JOURNAL OF MECHANICAL SCIENCE AND TECHNOLOGY, 2014, 28 (01) :365-376
[9]  
Ghanbarian A, 2014, IRAN J HYDROGEN FUEL, V3, P1
[10]   A novel concept for convective heat transfer enhancement [J].
Guo, ZY ;
Li, DY ;
Wang, BX .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1998, 41 (14) :2221-2225