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.