Process integration and optimization of a solid oxide fuel cell - Gas turbine hybrid cycle fueled with hydrothermally gasified waste biomass

被引:48
作者
Facchinetti, Emanuele [1 ]
Gassner, Martin [1 ]
D'Amelio, Matilde [1 ]
Marechal, Francois [1 ]
Favrat, Daniel [1 ]
机构
[1] Ecole Polytech Fed Lausanne, EPFL LENI IGM STI, CH-1015 Lausanne, Switzerland
关键词
Hydrothermal biomass gasification; Hybrid cycle; SOFC; Process design; Process integration; Optimization; CONTINUOUS SALT PRECIPITATION; EQUATION-OF-STATE; SUPERCRITICAL-WATER; CH4-CO2-H2O SYSTEM; GASIFICATION; PART; MODEL; 1000-DEGREES-C; SOLUBILITY; SEPARATION;
D O I
10.1016/j.energy.2012.02.059
中图分类号
O414.1 [热力学];
学科分类号
摘要
Due to its suitability for using wet biomass, hydrothermal gasification is a promising process for the valorization of otherwise unused waste biomass to synthesis gas and biofuels. Solid oxide fuel cell (SOFC) based hybrid cycles are considered as the best candidate for a more efficient and clean conversion of (bio) fuels. A significant potential for the integration of the two technologies is expected since hydrothermal gasification requires heat at 673-773 K, whereas SOFC is characterized by heat excess at high temperature due to the limited electrochemical fuel conversion. This work presents a systematic process integration and optimization of a SOFC-gas turbine (GT) hybrid cycle fueled with hydrothermally gasified waste biomass. Several design options are systematically developed and compared through a thermodynamic optimization approach based on First Law and exergy analysis. The work demonstrates the considerable potential of the system that allows for converting wet waste biomass into electricity at a First Law efficiency of up to 63%, while simultaneously enabling the separation of biogenic carbon dioxide for further use or sequestration. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:408 / 419
页数:12
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