Computational fluid dynamics modeling of a solid oxide electrolyzer cell for hydrogen production

被引:103
作者
Ni, Meng [1 ]
机构
[1] Hong Kong Polytech Univ, Dept Bldg & Real Estate, Kowloon, Hong Kong, Peoples R China
关键词
Heat and mass transfer; Solid oxide fuel cell (SOFC); High temperature steam electrolysis; Electrochemistry; Porous media; Transport phenomena; HIGH-TEMPERATURE ELECTROLYSIS; FUEL-CELL; STEAM ELECTROLYSIS; WATER-VAPOR; TRANSPORT PHENOMENA; HEAT/MASS TRANSFER; COUPLED TRANSPORT; DUCTS RELEVANT; ENERGY; ANODE;
D O I
10.1016/j.ijhydene.2009.07.080
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A 2D computational fluid dynamics (CFD) model was developed to study the performance of a planar solid oxide electrolyzer cell (SOEC) for hydrogen production. The governing equations for mass continuity, momentum conservation, energy conservation and species conservation were discretized with the finite volume method (FVM). The coupling of velocity and pressure was treated with the SIMPLEC (Semi-Implicit Method for Pressure Linked Equations - Consistent) algorithm. Simulations were performed to investigate the effects of operating/structural parameters on heat/mass transfer and the electric characteristics of a planar SOEC. It is found that the gas velocity at the cathode increases significantly along the main flow channel, as the increase in H-2 molar fraction decreases the density and viscosity of the gas mixture at the cathode. It is also found that increasing the inlet gas velocity can enhance the SOEC performance. Another important finding is that the electrode porosity has small effect on SOEC performance. The results of this paper provide better understanding on the coupled heat/mass transfer and electrochemical reaction phenomena in an SOEC. The model developed can serve as a useful tool for SOEC design optimization. (C) 2009 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:7795 / 7806
页数:12
相关论文
共 54 条
[1]   HYDROGEN-PRODUCTION FROM HIGH-TEMPERATURE STEAM ELECTROLYSIS USING SOLAR-ENERGY [J].
ARASHI, H ;
NAITO, H ;
MIURA, H .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1991, 16 (09) :603-608
[2]   A robust model and numerical approach for solving solid oxide fuel cell (SOFC) problems [J].
Arpino, F. ;
Carotenuto, A. ;
Massarotti, N. ;
Nithiarasu, P. .
INTERNATIONAL JOURNAL OF NUMERICAL METHODS FOR HEAT & FLUID FLOW, 2008, 18 (7-8) :811-834
[3]   Thermodynamic assessment of geothermal energy use in hydrogen production [J].
Balta, M. Tolga ;
Dincer, Ibrahim ;
Hepbasli, Arif .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (07) :2925-2939
[4]   High temperature water electrolysis in solid oxide cells [J].
Brisse, Annabelle ;
Schefold, Josef ;
Zahid, Mohsine .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (20) :5375-5382
[5]   Polarization effects in electrolyte/electrode-supported solid oxide fuel cells [J].
Chan, SH ;
Xia, ZT .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 2002, 32 (03) :339-347
[6]   Anode micro model of solid oxide fuel cell [J].
Chan, SH ;
Xia, ZT .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2001, 148 (04) :A388-A394
[7]   A complete polarization model of a solid oxide fuel cell and its sensitivity to the change of cell component thickness [J].
Chan, SH ;
Khor, KA ;
Xia, ZT .
JOURNAL OF POWER SOURCES, 2001, 93 (1-2) :130-140
[8]   HIGH-TEMPERATURE ELECTROLYSIS OF WATER-VAPOR - STATUS OF DEVELOPMENT AND PERSPECTIVES FOR APPLICATION [J].
DONITZ, W ;
ERDLE, E .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1985, 10 (05) :291-295
[9]   ELECTROCHEMICAL HIGH-TEMPERATURE TECHNOLOGY FOR HYDROGEN-PRODUCTION OR DIRECT ELECTRICITY-GENERATION [J].
DONITZ, W ;
DIETRICH, G ;
ERDLE, E ;
STREICHER, R .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1988, 13 (05) :283-287
[10]   Three-dimensional numerical simulation for various geometries of solid oxide fuel cells [J].
Ferguson, JR ;
Fiard, JM ;
Herbin, R .
JOURNAL OF POWER SOURCES, 1996, 58 (02) :109-122