Three-Dimensional Computational Fluid Dynamics Modelling of Oxygen Bubble Transport in Polymer Electrolyte Membrane Electrolyzer Porous Transport Layers

被引:84
作者
Arbabi, F. [1 ]
Montazeri, H. [1 ]
Abouatallah, R. [2 ]
Wang, R. [2 ]
Bazylak, A. [1 ]
机构
[1] Univ Toronto, Fac Appl Sci & Engn, Thermofluids Energy & Adv Mat TEAM Lab, Dept Mech & Ind Engn,Inst Sustainable Energy, Toronto, ON M5S 3G8, Canada
[2] Hydrogenics Corp, Adv Stack Technol, Mississauga, ON L5T 2N6, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
PEM ELECTROLYZER; 2-PHASE FLOW; WATER ELECTROLYSIS; MULTIPHASE FLOWS; IN-SITU; HYDROGEN; SIMULATION; POROSITY; SURFACE; LIQUID;
D O I
10.1149/2.0091611jes
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
A three-dimensional (3D), two-phase numerical model was developed and presented as a useful tool for investigating oxygen bubble propagation in porous transport layers (PTLs) (otherwise known as gas diffusion layers (GDLs)) of polymer electrolyte membrane (PEM) electrolyzers. The volume-of-fluid (VoF) technique was employed to simulate the liquid-gas interface movement through liquid-saturated porous media designed to be representative of PEM electrolyzer PTLs. The circulation of the liquid within the channel and the porous domain was included in the model. Bubble propagation patterns and bulk saturations for porous material representations of commonly used PTLs were determined as a function of time leading up to the moment of breakthrough. Previously conducted experimental microfluidic investigations were used for model validation, and it was found that the numerical results were in good agreement with the numerical predictions. The validated model was used to calculate pressure variations in bubbles during propagation, and the highest threshold capillary pressure corresponding to a critical throat was introduced as a means to measure the efficacy of oxygen bubble removal. The information obtained from the developed numerical tool can be used for designing and evaluating PTL microstructures for next generation electrolyzer materials. (C) 2016 The Electrochemical Society. All rights reserved.
引用
收藏
页码:F3062 / F3069
页数:8
相关论文
共 50 条
[1]   Hydrodynamics of gas-liquid Taylor flow in rectangular microchannels [J].
Abadie, Thomas ;
Aubin, Joelle ;
Legendre, Dominique ;
Xuereb, Catherine .
MICROFLUIDICS AND NANOFLUIDICS, 2012, 12 (1-4) :355-369
[2]  
[Anonymous], 2012, POROUS MEDIA FLUID T
[3]  
[Anonymous], 1980, Numerical heat transfer and fluid flow
[4]   Visualizing Bubble Flows in Electrolyzer GDLs using Microfluidic Platforms [J].
Arbabi, F. ;
Kalantarian, A. ;
Abouatallah, R. ;
Wang, R. ;
Wallace, J. ;
Bazylak, A. .
POLYMER ELECTROLYTE FUEL CELLS 13 (PEFC 13), 2013, 58 (01) :907-918
[5]   Feasibility study of using microfluidic platforms for visualizing bubble flows in electrolyzer gas diffusion layers [J].
Arbabi, F. ;
Kalantarian, A. ;
Abouatallah, R. ;
Wang, R. ;
Wallace, J. S. ;
Bazylak, A. .
JOURNAL OF POWER SOURCES, 2014, 258 :142-149
[6]  
Barton IE, 1998, INT J NUMER METH FL, V26, P459, DOI 10.1002/(SICI)1097-0363(19980228)26:4<459::AID-FLD645>3.0.CO
[7]  
2-U
[8]   A CONTINUUM METHOD FOR MODELING SURFACE-TENSION [J].
BRACKBILL, JU ;
KOTHE, DB ;
ZEMACH, C .
JOURNAL OF COMPUTATIONAL PHYSICS, 1992, 100 (02) :335-354
[9]   The use of Volume of Fluid technique to analyze multiphase flows: Specific case of bubble rising in still liquids [J].
Cano-Lozano, J. C. ;
Bolanos-Jimenez, R. ;
Gutierrez-Montes, C. ;
Martinez-Bazan, C. .
APPLIED MATHEMATICAL MODELLING, 2015, 39 (12) :3290-3305
[10]   A comprehensive review on PEM water electrolysis [J].
Carmo, Marcelo ;
Fritz, David L. ;
Merge, Juergen ;
Stolten, Detlef .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (12) :4901-4934