Exergy-Based and Economic Evaluation of Liquefaction Processes for Cryogenics Energy Storage

被引:55
作者
Hamdy, Sarah [1 ]
Moser, Francisco [2 ]
Morosuk, Tatiana [2 ]
Tsatsaronis, George [2 ]
机构
[1] Tech Univ Berlin, Energy Engn Dept, D-10587 Berlin, Germany
[2] Tech Univ Berlin, Inst Energy Engn, D-10587 Berlin, Germany
关键词
cryogenic energy storage; air liquefaction; exergy analysis; economic analysis; exergoeconomic analysis; THERMODYNAMIC ANALYSIS; PERFORMANCE; SYSTEM; COLD; RECOVERY; HEAT;
D O I
10.3390/en12030493
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
Cryogenics-based energy storage (CES) is a thermo-electric bulk-energy storage technology, which stores electricity in the form of a liquefied gas at cryogenic temperatures. The charging process is an energy-intensive gas liquefaction process and the limiting factor to CES round trip efficiency (RTE). During discharge, the liquefied gas is pressurized, evaporated and then super-heated to drive a gas turbine. The cold released during evaporation can be stored and supplied to the subsequent charging process. In this research, exergy-based methods are applied to quantify the effect of cold storage on the thermodynamic performance of six liquefaction processes and to identify the most cost-efficient process. For all liquefaction processes assessed, the integration of cold storage was shown to multiply the liquid yield, reduce the specific power requirement by 50-70% and increase the exergetic efficiency by 30-100%. The Claude-based liquefaction processes reached the highest exergetic efficiencies (76-82%). The processes reached their maximum efficiency at different liquefaction pressures. The Heylandt process reaches the highest RTE (50%) and the lowest specific power requirement (1021 kJ/kg). The lowest production cost of liquid air (18.4 Euro/ton) and the lowest specific investment cost (<700 Euro/kW(char)) were achieved by the Kapitza process.
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页数:19
相关论文
共 37 条
[1]   Performance evaluation of various cryogenic energy storage systems [J].
Abdo, Rodrigo F. ;
Pedro, Hugo T. C. ;
Koury, Ricardo N. N. ;
Machado, Luiz ;
Coimbra, Carlos F. M. ;
Porto, Matheus P. .
ENERGY, 2015, 90 :1024-1032
[2]   Thermodynamic analysis of energy storage with a liquid air Rankine cycle [J].
Ameel, Bernd ;
T'Joen, Christophe ;
De Kerpel, Kathleen ;
De Jaeger, Peter ;
Huisseune, Henk ;
Van Belleghem, Marnix ;
De Paepe, Michel .
APPLIED THERMAL ENGINEERING, 2013, 52 (01) :130-140
[3]  
Barron R.F., 1985, Cryogenic systems, V2
[4]  
Bejan A., 1995, Thermal Design and Optimization
[5]   A preliminary study on the optimal configuration and operating range of a "microgrid scale" air liquefaction plant for Liquid Air Energy Storage [J].
Borri, E. ;
Tafone, A. ;
Romagnoli, A. ;
Comodi, G. .
ENERGY CONVERSION AND MANAGEMENT, 2017, 143 :275-285
[6]  
Brett Gareth, 2014, EPJ Web of Conferences, V79, DOI 10.1051/epjconf/20147903002
[7]  
Chen H., 2006, US Patent, Patent No. [EP1989400A1, 1989400]
[8]   Progress in electrical energy storage system: A critical review [J].
Chen, Haisheng ;
Cong, Thang Ngoc ;
Yang, Wei ;
Tan, Chunqing ;
Li, Yongliang ;
Ding, Yulong .
PROGRESS IN NATURAL SCIENCE-MATERIALS INTERNATIONAL, 2009, 19 (03) :291-312
[9]   Thermodynamic analysis of a liquid air energy storage system [J].
Guizzi, Giuseppe Leo ;
Manno, Michele ;
Tolomei, Ludovica Maria ;
Vitali, Ruggero Maria .
ENERGY, 2015, 93 :1639-1647
[10]  
Hamdy S., 2019, CRYOGENICS UNPUB