Black Hole-Inspired Optimal Design of Biomethane Liquefaction Process for Small-Scale Applications

被引:6
|
作者
He, Tianbiao [1 ]
Qyyum, Muhammad Abdul [2 ]
Zhou, Zhongming [1 ]
Ahmad, Ashfaq [3 ]
Rehan, Mohammad [4 ]
Nizami, Abdul-Sattar [5 ]
Lee, Moonyong [2 ]
机构
[1] China Univ Petr East China, Coll Pipeline & Civil Engn, Dept Gas Engn, Qingdao, Peoples R China
[2] Yeungnam Univ, Sch Chem Engn, Gyaongsan Si, South Korea
[3] COMSATS Univ Islamabad, Dept Comp Sci, Lahore, Pakistan
[4] King Abdulaziz Univ, Ctr Excellence Environm Studies, Jeddah, Saudi Arabia
[5] Govt Coll Univ, Sustainable Dev Study Ctr, Lahore, Pakistan
基金
新加坡国家研究基金会; 中国国家自然科学基金;
关键词
biomethane; liquefied biomethane; single mixed refrigerant; optimization; exergy destruction analysis; renewable LNG; liquid biogas; energy consumption minimization;
D O I
10.3389/fenrg.2021.656165
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
Biomethane is regarded as a promising renewable energy source, with great potential to satisfy the growth of energy demands and to reduce greenhouse gas emissions. Liquefaction is a suitable approach for long distances and overseas transportation of biomethane; however, it is energy-intensive due to its cryogenic working condition. The major challenge is to design a high-energy efficiency liquefaction process with simple operation and configuration. A single mixed refrigerant biomethane liquefaction process adopting the cryogenic liquid turbine for small-scale production has been proposed in this study to address this issue. The optimal design corresponding to minimal energy consumption was obtained through the black-hole-based optimization algorithm. The effect of the minimum internal temperature approach (MITA) in the main cryogenic heat exchanger on the biomethane liquefaction process performance was investigated. The study results indicated that the specific energy consumption of modified case 2 with MITA of 2 degrees C was 0.3228 kWh/kg with 21.01% reduction compared to the published base case. When the MITA decreased to 1 degrees C, the specific power of modified case 1 reduced to 0.3162 kWh/kg, which was 24.96% lower than the base case. In terms of exergy analysis, the total exergy destruction of the modified cases 1, 2, and 3 was 31.28%, 22.27%, and 17.51% lower than the base case, respectively. This study's findings suggested that introducing the cryogenic liquid turbine to the single mixed refrigerant-based biomethane liquefaction process could reduce the specific energy consumption and total exergy destruction significantly. Therefore, this study could provide a viable path for designing and improving the small-scale biomethane liquefaction process.
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页数:15
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