Thermodynamic analysis of a novel integrated biomass pyrolysis-solid oxide fuel cells-combined heat and power system for co-generation of biochar and power

被引:1
|
作者
Kuo, Po-Chih [1 ,2 ]
Illathukandy, Biju [1 ,3 ]
Ozdemir, Faruk [1 ]
Woudstra, Theo [1 ]
Aravind, P. V. [4 ,5 ,6 ]
机构
[1] Delft Univ Technol, Fac 3mE, Proc & Energy Dept, Delft, Netherlands
[2] Univ Tokyo, Inst Ind Sci, Tokyo, Japan
[3] Indian Inst Technol, Ctr Rural Dev & Technol, Delhi, India
[4] Univ Groningen, Energy & Sustainabil Res Inst Groningen, Fac Sci & Engn, Groningen, Netherlands
[5] Delft Univ Technol, Climate Inst, Delft, Netherlands
[6] Delft Univ Technol, Water Engn, CiTG, Delft, Netherlands
来源
基金
日本学术振兴会;
关键词
biochar; SOFC; biomass pyrolysis; process integration; thermodynamic analysis; negative emissions technologies; EXERGY ANALYSIS; SLOW PYROLYSIS; CORN STOVER; SOFC; GASIFICATION; PERFORMANCE; GENERATION; EFFICIENCY; GAS; SIMULATION;
D O I
10.3389/fenrg.2022.731191
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Biochar derived from pyrolysis or gasification has been gaining significant attention in the recent years due to its potential wide applications for the development of negative emissions technologies. A new concept was developed for biochar and power co-generation system using a combination of biomass pyrolysis (BP) unit, solid oxide fuel cells (SOFCs), and a combined heat and power (CHP) system. A set of detailed experimental data of pyrolysis product yields was established in Aspen Plus to model the BP process. The impacts of various operating parameters including current density (j), fuel utilization factor (U-f), pyrolysis gas reforming temperature (T-reformer), and biochar split ratio (R-biochar) on the SOFC and overall system performances in terms of energy and exergy analyses were evaluated. The simulation results indicated that increasing the U-f, T-reformer, and R-biochar can favorably improve the performances of the BP-SOFC-CHP system. As a whole, the overall electrical, energy and exergy efficiencies of the BP-SOFC-CHP system were in the range of 8-14%, 76-78%, and 71-74%, respectively. From the viewpoint of energy balance, burning the reformed pyrolysis gas can supply enough energy demand for the process to achieve a stand-alone BP-SOFC-CHP plant. In case of a stand-alone system, the overall electrical, energy and exergy efficiencies were 5.4, 63.9 and 57.8%, respectively, with a biochar yield of 31.6%.
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页数:18
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