Optimized multi-criteria performance of a poly-generation layout including a Stirling engine and a supercritical Brayton cycle using biogas and methane as two potential fuels of a topping gas turbine cycle

被引:1
|
作者
Wang, Dan [1 ,2 ]
Jasim, Dheyaa J. [3 ]
Zoghi, Mohammad [4 ]
Habibi, Hamed [4 ]
机构
[1] Qiannan Normal Univ Nationalities, Sch Math & Stat, Duyun 558000, Peoples R China
[2] Key Lab Complex Syst & Intelligent Optimizat Guizh, Duyun 558000, Peoples R China
[3] Al Amarah Univ Coll, Dept Petr Engn, Maysan, Iraq
[4] Univ Guilan, Fac Mech Engn, Rasht, Iran
关键词
Waste heat recovery; Gas turbine; Biogas; Stirling engine; Poly-generation; Supercritical Brayton cycle; ORGANIC RANKINE-CYCLE; THERMOECONOMIC ANALYSIS; EXERGOECONOMIC ANALYSIS; HYDROGEN-PRODUCTION; ECONOMIC-EVALUATION; PEM ELECTROLYZER; HEAT-RECOVERY; POWER-SYSTEM; NATURAL-GAS; DRIVEN;
D O I
10.1016/j.energy.2024.133172
中图分类号
O414.1 [热力学];
学科分类号
摘要
The combination of a supercritical Brayton cycle, an absorption chiller, a Stirling engine, a reverse osmosis desalination system, and a proton exchange membrane electrolyzer is investigated for waste heat recovery of a topping gas turbine cycle. The required electricity for hydrogen and freshwater production is supplied by the Stirling engine and supercritical Brayton cycle, respectively. In addition, the output power is provided by the gas turbine cycle, and the exiting cold stream of the Stirling engine is considered hot water for domestic utilization. A comparison is made between biogas and pure methane as two possible fuels for the system. Energy and exergy analyses, economic analysis using the specific exergy costing approach, and environmental analysis considering the carbon dioxide emissions are employed in the study. The three-objective optimization of the configuration discloses an exergy efficiency (eta(ex)) of 39.49 % and 39.85 % in the cases of biogas and methane, respectively. The proposed system can improve eta(ex) by 6.18 % points compared to the stand-alone GTC. The specific cost of poly- generation (c poly ) and the total cost rate ((sic)(tot)) are obtained as 25.92 $ GJ(-1)- 1 and 249.5 $ h(-1) in the biogas mode, while these values are calculated as 36.75 $ GJ(-1) and 336.7 $ h(-1) in the methane case. The environmental cost rate ((sic)(env)) of the system is 24.78 $ h(-1) in the case of biogas and 17.47 $ h(-1) in the methane mode. The results confirm the superiority of the methane case from the environmental viewpoint over biogas. However, the low values of c poly and (sic)(tot) in the biogas case indicate that biogas is superior to methane from a general standpoint. The utilization of the present setup for waste heat recovery of biogas-driven GTCs is recommended due to the higher eta(ex) than the previous layouts.
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页数:18
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