Optimization of reforming catalyst distribution in a cross-flow molten carbonate fuel cell with direct internal reforming

被引:16
|
作者
Heidebrecht, P
Sundmacher, K
机构
[1] Max Planck Inst Dynam Complex Tech Syst, D-39106 Magdeburg, Germany
[2] Univ Magdeburg, Proc Syst Engn, D-39106 Magdeburg, Germany
关键词
D O I
10.1021/ie048759x
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Two optimization procedures of a molten carbonate fuel cell (MCFC) with direct internal reforming are presented. First, optimal operating conditions such as the amounts of feed gas, water, and air are calculated for a given cell current in order to obtain optimal electric efficiencies. An optimal current-voltage curve for the system is obtained by repeating this optimization for various cell currents. The second optimization balances the cooling effect of the endothermic reforming process and the heat-producing electrochemical reactions inside the cell in order to achieve a more homogeneous temperature profile. This is realized by optimization of the spatially distributed reforming catalyst density. A repeated calculation of the optimal current-voltage curve shows a significant increase of the electric efficiency by this measure. Both optimization procedures are based on a cross-flow MCFC model and consider several constraints concerning temperature, cell voltage, and carbonization.
引用
收藏
页码:3522 / 3528
页数:7
相关论文
共 50 条
  • [1] Dynamic model of a cross-flow molten carbonate fuel cell with direct internal reforming
    Heidebrecht, P
    Sundmacher, K
    JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2005, 152 (11) : A2217 - A2228
  • [2] Direct internal reforming molten carbonate fuel cell with core-shell catalyst
    Wang, Pengjie
    Zhou, Li
    Li, Guanglong
    Lin, Huaxin
    Shao, Zhigang
    Zhang, Xiongfu
    Yi, Baolian
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (03) : 2588 - 2595
  • [3] Development of an internal reforming molten carbonate fuel cell stack
    Shinoki, T
    Matsumura, M
    Sasaki, A
    IEEE TRANSACTIONS ON ENERGY CONVERSION, 1995, 10 (04) : 722 - 729
  • [4] Performance of internal and external reforming molten carbonate fuel cell systems
    Musa, A.
    Steeman, H. J.
    De Paepe, M.
    JOURNAL OF FUEL CELL SCIENCE AND TECHNOLOGY, 2007, 4 (01): : 65 - 71
  • [5] MOLTEN-CARBONATE FUEL-CELL WITH INDIRECT INTERNAL REFORMING
    FRENI, S
    AQUINO, M
    PASSALACQUA, E
    JOURNAL OF POWER SOURCES, 1994, 52 (01) : 41 - 47
  • [6] INTERNAL REFORMING FOR MOLTEN CARBONATE FUEL-CELLS
    LEDJEFF, K
    ROHRBACH, T
    SCHAUMBERG, G
    BERICHTE DER BUNSEN-GESELLSCHAFT-PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1990, 94 (09): : 956 - 960
  • [7] Porous ceramic membranes for direct internal reforming molten carbonate fuel cells
    Passalacqua, E
    Freni, S
    Barone, F
    Patti, A
    MATERIALS LETTERS, 1996, 29 (1-3) : 177 - 183
  • [8] Dynamic simulation of direct reforming molten carbonate fuel cell system
    Lukas, MD
    Lee, KY
    Ghezel-Ayagh, H
    IEEE POWER ENGINEERING SOCIETY - 1999 WINTER MEETING, VOLS 1 AND 2, 1999, : 113 - 116
  • [9] DEVELOPMENT OF INDIRECT INTERNAL REFORMING MOLTEN-CARBONATE FUEL-CELL
    OHTSUKI, J
    SEKI, T
    MIYAZAKI, M
    SASAKI, A
    ELECTRICAL ENGINEERING IN JAPAN, 1995, 115 (03) : 64 - 75
  • [10] Hydrogen produced from ethanol for internal reforming molten carbonate fuel cell
    Cavallaro, S
    Mondello, N
    Freni, S
    JOURNAL OF POWER SOURCES, 2001, 102 (1-2) : 198 - 204