Performance evaluation of an integrated small-scale SOFC-biomass gasification power generation system

被引:56
|
作者
Wongchanapai, Suranat [1 ]
Iwai, Hiroshi [1 ]
Saito, Motohiro [1 ]
Yoshida, Hideo [1 ]
机构
[1] Kyoto Univ, Dept Aeronaut & Astronaut, Sakyo Ku, Kyoto 6068501, Japan
关键词
Solid oxide fuel cell; Biomass gasification; System analysis; Power generation system; Exergy analysis; OXIDE FUEL-CELL; EQUILIBRIUM-MODEL; WASTE GASIFIER; HYBRID SYSTEM; PREDICTION; PLANAR; IMPACT; ANODES; CYCLE; MGT;
D O I
10.1016/j.jpowsour.2012.05.098
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
The combination of biomass gasification and high-temperature solid oxide fuel cells (SOFCs) offers great potential as a future sustainable power generation system. In order to provide insights into an integrated small-scale SOFC-biomass gasification power generation system, system simulation was performed under diverse operating conditions. A detailed anode-supported planar SOFC model under co-flow operation and a thermodynamic equilibrium for biomass gasification model were developed and verified by reliable experimental and simulation data. The other peripheral components include three gas-to-gas heat exchangers (HXs), heat recovery steam generator (HRSG), burner, fuel and air compressors. To determine safe operating conditions with high system efficiency, energy and exergy analysis was performed to investigate the influence through detailed sensitivity analysis of four key parameters, e.g. steam-to-biomass ratio (STBR), SOFC inlet stream temperatures, fuel utilization factor (U-f) and anode off-gas recycle ratio (AGR) on system performance. Due to the fact that SOFC stack is accounted for the most expensive part of the initial investment cost, the number of cells required for SOFC stack is economically optimized as well. Through the detailed sensitivity analysis, it shows that the increase of STBR positively affects SOFC while gasifier performance drops. The most preferable operating STBR is 1.5 when the highest system efficiencies and the smallest number of cells. The increase in SOFC inlet temperature shows negative impact on system and gasifier performances while SOFC efficiencies are slightly increased. The number of cells required for SOFC is reduced with the increase of SOFC inlet temperature. The system performance is optimized for U-f of 0.75 while SOFC and system efficiencies are the highest with the smallest number of cells. The result also shows the optimal anode off-gas recycle ratio of 0.6. Regarding with the increase of anode off-gas recycle ratio, there is a trade-off between overall efficiencies and the number of SOFC cells. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:314 / 322
页数:9
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