Pre-reforming of natural gas in solid oxide fuel-cell systems
被引:66
作者:
Peters, R
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机构:
Forschungszentrum Julich, Inst Mat & Proc Energy Syst Energy Proc Engn IWV3, D-52425 Julich, GermanyForschungszentrum Julich, Inst Mat & Proc Energy Syst Energy Proc Engn IWV3, D-52425 Julich, Germany
Peters, R
[1
]
Riensche, E
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机构:
Forschungszentrum Julich, Inst Mat & Proc Energy Syst Energy Proc Engn IWV3, D-52425 Julich, GermanyForschungszentrum Julich, Inst Mat & Proc Energy Syst Energy Proc Engn IWV3, D-52425 Julich, Germany
Riensche, E
[1
]
Cremer, P
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机构:
Forschungszentrum Julich, Inst Mat & Proc Energy Syst Energy Proc Engn IWV3, D-52425 Julich, GermanyForschungszentrum Julich, Inst Mat & Proc Energy Syst Energy Proc Engn IWV3, D-52425 Julich, Germany
Cremer, P
[1
]
机构:
[1] Forschungszentrum Julich, Inst Mat & Proc Energy Syst Energy Proc Engn IWV3, D-52425 Julich, Germany
steam reforming;
pre-reformer;
anode gas recycling;
solid oxide fuel cells;
D O I:
10.1016/S0378-7753(99)00440-1
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:
Several measures concerning fuel processing in a solid oxide fuel cell (SOFC) system offer the possibility of significant cost reduction and higher system efficiencies. For SOFC systems, the ratio between internal and pre-reforming has to be optimized on the basis of experimental performance data. Furthermore, anode gas recycling by an injector in front of the pre-reformer can eliminate the steam generator and the corresponding heat of evaporation. A detailed study is carried out on pre-reforming in a reformer of considerable size (10 kW(el)). Simulating anode gas recycling with an injector, the influence of carbon dioxide on reactor performance was studied. Also, the dependence of the methanol conversion on mass flow and temperature will be discussed. In addition, some results concerning the dynamic behaviour of the pre-reformer are given. (C) 2000 Elsevier Science S.A. All rights reserved.