Effect of operation parameters on performance of tubular solid oxide fuel cell

被引:27
作者
Jia, Junxi [1 ]
Jiang, Renqiu [1 ]
Shen, Shengqiang [2 ]
Abudula, Abuliti [3 ]
机构
[1] Harbin Engn Univ, Coll Power & Energy Engn, Harbin 150001, Peoples R China
[2] Dalian Univ Technol, Sch Energy & Power Engn, Dalian 116024, Peoples R China
[3] Aomori Ind Res Ctr, Aomori 0300113, Japan
关键词
tubular solid oxide fuel cell; electrochemical reaction; heat and mass transfer; simulation;
D O I
10.1002/aic.11372
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A simulation model is developed to analyze steady state and transient operation of a tubular solid oxide fuel cell (SOFC). The performance of the tubular SOFC is compared when the operation parameters such as inlet fuel temperature, inlet oxidant temperature, and inlet oxidant flow rate are changed, respectively. The model includes both electrochemical model and thermal model. The electrochemical model includes the Nernst potential, ohmic polarization, activation polarization, and concentration polarization. The thermal model includes the heat transfer by conduction, convention, and radiation. An analysis is carried out to investigate the effects of the different operation parameters on the hot spot, solid temperature gradient at the steady state, and the response time at the transient state. Numerical results show that the performance of tubular SOFC due to the change of the different operation parameters is different at the steady state. For the transient response such as the same step increase in cell current density, the response time required for the new steady state is different as different operation parameters are changed. (c) 2007 American Institute of Chemical Engineers.
引用
收藏
页码:554 / 564
页数:11
相关论文
共 28 条
[11]  
HIRSOCHENHOFER JH, 2000, FUEL CELL HDB
[12]  
JUNXI J, 2005, CHEM RES CHINESE U, V21, P577
[13]  
JUNXI J, 2005, J ENERGY INST, V78, P76
[14]  
JUNXI J, 2004, ACTA ENERGIAE SOLARI, V25, P457
[15]  
KEYS WM, 1980, CONVECTIVE HEAT MASS
[16]   A numerical model coupling the heat and gas species' transport processes in a tubular SOFC [J].
Li, PW ;
Schaefer, L ;
Chyu, MK .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 2004, 126 (02) :219-229
[17]   Simulation of the chemical/electrochemical reactions and heat/mass transfer for a tubular SOFC in a stack [J].
Li, PW ;
Chyu, MK .
JOURNAL OF POWER SOURCES, 2003, 124 (02) :487-498
[18]   Internal reforming solid oxide fuel cell-gas turbine combined cycles (IRSOFC-GT): Part A - Cell model and cycle thermodynamic analysis [J].
Massardo, AF ;
Lubelli, F .
JOURNAL OF ENGINEERING FOR GAS TURBINES AND POWER-TRANSACTIONS OF THE ASME, 2000, 122 (01) :27-35
[19]   Numerical analysis of output characteristics of tubular SOFC with internal reformer [J].
Nagata, S ;
Momma, A ;
Kato, T ;
Kasuga, Y .
JOURNAL OF POWER SOURCES, 2001, 101 (01) :60-71
[20]   Two-dimensional transient model of a cascaded micro-tubular solid oxide fuel cell fed with methane [J].
Nehter, Pedro .
JOURNAL OF POWER SOURCES, 2006, 157 (01) :325-334