Optimization of a 200 kW SOFC cogeneration power plant. Part II: variation of the flowsheet

被引:56
作者
Riensche, E
Meusinger, J
Stimming, U
Unverzagt, G
机构
[1] Forschungszentrum Julich, Inst Energieverfahrenstech, D-52425 Julich, Germany
[2] Tech Univ Munich, Inst Festkorperphys & Tech Phys, D-85747 Garching, Germany
[3] Deutsch Shell AG, D-50972 Cologne, Germany
关键词
solid oxide fuel cell; cogeneration; cost analysis plant optimization;
D O I
10.1016/S0378-7753(97)02726-2
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
An energetic and economic analysis of a decentralized natural gas-fuelled solid oxide fuel cell (SOFC) power plant in the range of 200 kW capacity is carried out. All calculations start from a basic plant concept with a simple flowsheet and a basic parameter set of SOFC operation and economic data. Changes in costs of electricity and plant efficiencies are determined for variations of the plant concept. Flowsheets with gas recycling by blowers or jet boosters are described. Cathode gas recycling by jet boosters turns out to be more advantageous with respect to the costs of electricity than gas recycling by hot gas fans. The influence of pressure drop in the cathode gas circuit is analyzed. In case of anode gas recycling an internal steam circuit exists. This has the advantage that the external steam generator is eliminated and that the steam concentration in the exhaust gas is reduced. Therefore, a higher amount of excess heat can be used. Removal of useful heat at higher temperature levels diminishes the driving temperature differences and enlarges the heat exchange area of the recuperative heat exchangers located downstream. (C) 1998 Elsevier Science S.A.
引用
收藏
页码:306 / 314
页数:9
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