Validation of a mathematical model using an industrial MCFC plant

被引:9
作者
Gundermann, M.
Heidebrecht, P.
Sundmacher, K.
机构
[1] Otto von Guericke Univ, D-39106 Magdeburg, Germany
[2] Max Planck Inst Dynam Complex Tech Syst, D-39106 Magdeburg, Germany
来源
JOURNAL OF FUEL CELL SCIENCE AND TECHNOLOGY | 2006年 / 3卷 / 03期
关键词
MCFC; HotModule; mathematical model; parameter identification; validation;
D O I
10.1115/1.2211634
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
The parameter identification of a mathematical model of a molten carbonate fuel cell (MCFC) is presented. The model is spatially distributed in two dimensions and describes the strongly non-linear coupling of the temperature field and reactions inside a MCFC It contains a high number of unknown parameters that need to be validated by experimental means. Therefore, measurements from an industrial 250 kW fuel cell power plant are used. This validation approach requires an elaborate strategy, which is presented in detail. The resulting set of parameters can predict the behavior of the MCFC over a broad operating range with a very good precision. The validated model is an important basis for further process optimization and for control system design.
引用
收藏
页码:303 / 307
页数:5
相关论文
共 7 条
[1]   Operating experience with a 250 kWel molten carbonate fuel cell (MCFC) power plant [J].
Bischoff, M ;
Huppmann, G .
JOURNAL OF POWER SOURCES, 2002, 105 (02) :216-221
[2]  
GUNDERMANN M, 2005, TAG DECHEMA FACHS RE
[3]   Molten carbonate fuel cell (MCFC) with internal reforming: model-based analysis of cell dynamics [J].
Heidebrecht, P ;
Sundmacher, K .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (3-6) :1029-1036
[4]   Dynamic model of a cross-flow molten carbonate fuel cell with direct internal reforming [J].
Heidebrecht, P ;
Sundmacher, K .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2005, 152 (11) :A2217-A2228
[5]   Optimization of reforming catalyst distribution in a cross-flow molten carbonate fuel cell with direct internal reforming [J].
Heidebrecht, P ;
Sundmacher, K .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (10) :3522-3528
[6]  
HEIDEBRECHT P, 2005, FORTSCHRITT BERICHTE
[7]  
MANGOLD M, 2005, S NONL CONTR OBS DES