Performance assessment of a biomass-fuelled distributed hybrid energy system integrating molten carbonate fuel cell, externally fired gas turbine and supercritical carbon dioxide cycle

被引:65
作者
Roy, Dibyendu [1 ]
Samanta, Samiran [2 ]
Ghosh, Sudip [1 ]
机构
[1] Indian Inst Engn Sci & Technol, Dept Mech Engn, Howrah 711103, W Bengal, India
[2] Kalinga Inst Ind Technol, Sch Mech Engn, Bhubaneswar 24, Orissa, India
关键词
Biomass gasification; Molten carbonate fuel cell; s-CO2; cycle; Exergy analysis; Economic analysis; Environmental analysis; POWER-PLANT; MULTIOBJECTIVE OPTIMIZATION; HYDROGEN-PRODUCTION; TECHNOECONOMIC ASSESSMENT; THERMOECONOMIC ANALYSIS; THERMODYNAMIC ANALYSIS; EXERGY ANALYSIS; HEAT-RECOVERY; NATURAL-GAS; GASIFICATION;
D O I
10.1016/j.enconman.2020.112740
中图分类号
O414.1 [热力学];
学科分类号
摘要
This article proposes an innovative distributed hybrid power system where the biomass gasification technology is integrated with the molten carbonate fuel cell, an externally fired gas turbine, and a supercritical carbon dioxide cycle. The thermodynamic, economic and environmental performances of the proposed system are extensively studied to show the impact of the main operational and design parameters. The proposed small capacity hybrid power system yields the highest energy efficiency of 40.88%, which is close to the efficiency level of the large-scale biomass gasification based combined cycle system. The maximum exergetic efficiency of the proposed power system is estimated to be around 34.07%. The biomass gasifier (31.79%) contributes the highest amount of exergy destruction, followed by the primary heat exchanger (15.97%), combustion chamber (14.01%) and the molten carbonate fuel cell (12.53%) unit. The sensitivity analysis reveals that the cost of electricity can reach up to 0.1057 $/kWh. A comparative performance analysis, among other biomass-fueled power generation systems suggests that the developed power system yields better techno-economic performance than the other previously proposed system configurations. The environmental analysis reveals that the proposed plant can reduce maximum up to 1510 ton of CO2/year, which yields an environmental benefit of 21,901 $/year, in comparison to a fossil fuel-based plant of similar capacity.
引用
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页数:19
相关论文
共 86 条
[1]  
Alauddin ZA, 1996, THESIS
[2]   Prediction of the working parameters of a wood waste gasifier through an equilibrium model [J].
Altafini, CR ;
Wander, PR ;
Barreto, RM .
ENERGY CONVERSION AND MANAGEMENT, 2003, 44 (17) :2763-2777
[3]   Thermodynamic analysis of small-scale externally fired gas turbines and combined cycles using turbo-compound components for energy generation from solid biomass [J].
Amirante, Riccardo ;
De Palma, Pietro ;
Distaso, Elia ;
Tamburrano, Paolo .
ENERGY CONVERSION AND MANAGEMENT, 2018, 166 :648-662
[4]  
[Anonymous], 2015, BIOM HEAT POW TECHN
[5]   Thermoeconomic modeling and exergy analysis of a decentralized liquefied natural gas-fueled combined-cooling heating-and-power plant [J].
Arsalis, Alexandros ;
Alexandrou, Andreas .
JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2014, 21 :209-220
[6]   Energy and exergy analysis of a sugar cane bagasse gasifier integrated to a solid oxide fuel cell based on a quasi-equilibrium approach [J].
Arteaga-Perez, Luis E. ;
Casas-Ledon, Yannay ;
Perez-Bermudez, Raul ;
Peralta, Luis M. ;
Dewulf, Jo ;
Prins, Wolter .
CHEMICAL ENGINEERING JOURNAL, 2013, 228 :1121-1132
[7]   Decentralized combined heat and power production by two-stage biomass gasification and solid oxide fuel cells [J].
Bang-Moller, C. ;
Rokni, M. ;
Elmegaard, B. ;
Ahrenfeldt, J. ;
Henriksen, U. B. .
ENERGY, 2013, 58 :527-537
[8]   Optimum performance of a single effect desalination unit integrated with a SOFC system by multi-objective thermo-economic optimization based on genetic algorithm [J].
Beyrami, Javid ;
Chitsaz, Ata ;
Parham, Kiyan ;
Arild, Oystein .
ENERGY, 2019, 186
[9]   Modeling of hydrogen production process from biomass using oxygen blown gasification [J].
Bhattacharya, Atmadeep ;
Bhattacharya, Abhishek ;
Datta, Amitava .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (24) :18782-18790
[10]   Using MCFC for high efficiency CO2 capture from natural gas combined cycles: Comparison of internal and external reforming [J].
Campanari, Stefano ;
Manzolini, Giampaolo ;
Chiesa, Paolo .
APPLIED ENERGY, 2013, 112 :772-783