Performance evaluation of different bipolar plate designs of 3D planar anode-supported SOFCs

被引:41
作者
Bhattacharya, Deepra [1 ]
Mukhopadhyay, Jayanta [1 ]
Biswas, Nayan [2 ]
Basu, Rajendra Nath [1 ]
Das, Prasanta Kumar [2 ]
机构
[1] CSIR Cent Glass & Ceram Res Inst, Fuel Cell & Battery Div, Kolkata, India
[2] Indian Inst Technol, Dept Mech Engn, Kharagpur, W Bengal, India
关键词
SOFC modelling; Bipolar plate; Serpentine channel; Fuel utilisation; Cell performance; Parametric analysis; SOLID OXIDE FUEL; OPERATING-CONDITIONS; MASS-TRANSPORT; SHORT STACK; DUSTY-GAS; CELL; FLOW; OPTIMIZATION; CFD; CHANNELS;
D O I
10.1016/j.ijheatmasstransfer.2018.02.096
中图分类号
O414.1 [热力学];
学科分类号
摘要
The performance of Solid Oxide Fuel Cells (SOFCs) is highly sensitive to the fluid dynamics, the interfacial areas, and the residence time of the gases. These parameters are primarily dictated by the geometry of the channels carrying the fuel and the oxidant. However, not many investigations have been made to study the effect of bipolar plate designs on cell performance. We report a detailed comparative study of the performance characteristics of straight and serpentine channel geometries. Simulations of these two channels have been made taking into account fluid flow through the channels and the porous electrodes, multicomponent diffusion, heat transfer, charge transfer reaction kinetics and electrodynamics. Performance of each channel has been compared to in-house experimental data. Extensive parametric analyses have been carried out to evaluate the dependence of cell performance on fuel and air flow rates. Favourable operating ranges of hydrogen and air feeds have been estimated analytically taking into account fuel utilisation, cell temperature, channel pressure drops, and current density. It has been shown that serpentine geometries offer remarkably more uniform distribution of ionic current density, and significantly higher power output and fuel utilisation compared to straight channel geometries. However, these are accompanied by a penalty of pressure drop. This analysis can provide a useful guideline for selecting the channel geometry. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:382 / 396
页数:15
相关论文
共 47 条
[1]   3-DIMENSIONAL AND TIME-DEPENDENT SIMULATION OF A PLANAR SOLID OXIDE FUEL-CELL STACK [J].
ACHENBACH, E .
JOURNAL OF POWER SOURCES, 1994, 49 (1-3) :333-348
[2]   A 3D CFD model for predicting the temperature distribution in a full scale APU SOFC short stack under transient operating conditions [J].
Al-Masri, A. ;
Peksen, M. ;
Blum, L. ;
Stolten, D. .
APPLIED ENERGY, 2014, 135 :539-547
[3]   SOFC Cell Design Optimization Using the Finite Element Method Based CFD Approach [J].
Andersson, M. ;
Yuan, J. ;
Sunden, B. .
FUEL CELLS, 2014, 14 (02) :177-188
[4]   SOFC modeling considering electrochemical reactions at the active three phase boundaries [J].
Andersson, Martin ;
Yuan, Jinliang ;
Sunden, Bengt .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2012, 55 (04) :773-788
[5]  
[Anonymous], 2007, TRANSPORT PHENOMENA
[6]   Processing of high-performance anode-supported planar solid oxide fuel cell [J].
Basu, R. N. ;
Das Sharma, A. ;
Dutta, Atanu ;
Mukhopadhyay, J. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (20) :5748-5754
[7]   Computational analysis of IR-SOFC: Thermodynamic, electrochemical process and flow configuration dependency [J].
Choudhary, Tushar ;
Sanjay .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (02) :1259-1271
[8]  
COMSOL, 2017, COMSOL 5 3 DOC
[9]   Micro-modelling of solid oxide fuel cell electrodes [J].
Costamagna, P ;
Costa, P ;
Antonucci, V .
ELECTROCHIMICA ACTA, 1998, 43 (3-4) :375-394
[10]   Multicomponent diffusion [J].
Curtiss, CF ;
Bird, RB .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (07) :2515-2522