Comparative exergy and exergoeconomic analysis between liquid fuels production through chemical looping hydrogen generation and methane reforming with CO2

被引:31
作者
He, Yangdong [1 ,2 ]
Zhu, Lin [1 ]
Fan, Junming [2 ]
Li, Luling [1 ,2 ]
机构
[1] Southwest Petr Univ, Sch Chem & Chem Engn, Key Lab Gas Proc Engn, Chengdu 610500, Peoples R China
[2] China Shenzhen Gas Corp Ltd, Shenzhen 518040, Peoples R China
基金
中国国家自然科学基金;
关键词
Carbon utilization; Chemical looping hydrogen generation; Liquid fuels; Exergy analysis; Exergoeconomic analysis; CARBON-DIOXIDE; EFFICIENT UTILIZATION; POWER COGENERATION; PERFORMANCE; ENERGY; CYCLE; GAS; OPTIMIZATION; COMBUSTION; SIMULATION;
D O I
10.1016/j.enconman.2020.113239
中图分类号
O414.1 [热力学];
学科分类号
摘要
Recently, the concept of carbon utilization has been widely investigated to reduce greenhouse gas emissions and mitigate dependence on fossil fuels. For this purpose, two different carbon capture and utilization processes to produce liquid fuels, carbon looping cyclic reforming (CCR) and carbon dioxide hydrogenation based on chemical looping hydrogen generation (CH-CLHG), are introduced. This article aims to identify which utilization method holds more potential for future technical development. To achieve it, comprehensive thermodynamic, economic and exergoeconomic assessments are implemented. The results indicate that the exergy efficiency of CH-CLHG system is 3.84% more than that of CCR system, and the cost of liquid fuels production is 36.64% less. It is also suggested that CCR system is superior to CH-CLHG system in terms of the liquid fuels output. When the electricity price is below 0.068 $/kWh, the cost of liquid fuels of CCR system is more competitive than that of CH-CLHG system. Since the higher fuel cost and larger exergy destruction, CCR system's exergy destruction cost is more significant. In addition, the exergy destruction and exergy efficiency as well as exergoeconomic performance of each main component are presented in detail to reveal the cost formation process, and to find out the measure that would improve system efficiency and cost-effectiveness.
引用
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页数:11
相关论文
共 35 条
[1]   Exergoeconomic analysis and optimization of combined heat and power production: A review [J].
Abusoglu, Aysegul ;
Kanoglu, Mehmet .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2009, 13 (09) :2295-2308
[2]   Exergoeconomic analysis and multi objective optimization of performance of a Carbon dioxide power cycle driven by geothermal energy with liquefied natural gas as its heat sink [J].
Ahmadi, Mohammad H. ;
Mehrpooya, Mehdi ;
Pourfayaz, Fathollah .
ENERGY CONVERSION AND MANAGEMENT, 2016, 119 :422-434
[3]   Comparison between two methods of methanol production from carbon dioxide [J].
Anicic, B. ;
Trop, P. ;
Goricanec, D. .
ENERGY, 2014, 77 :279-289
[4]  
[Anonymous], 2018, Global Energy CO2 Status Report 2017
[5]   Assessing the potential of utilization and storage strategies for post-combustion CO2 emissions reduction [J].
Armstrong, Katy ;
Styring, Peter .
FRONTIERS IN ENERGY RESEARCH, 2015, 3 (MAR)
[6]   Exergy based performance analysis of hydrogen production from rice straw using oxygen blown gasification [J].
Bhattacharya, Atmadeep ;
Das, Anirban ;
Datta, Amitava .
ENERGY, 2014, 69 :525-533
[7]   Oxy-combustion of coal, lignite and biomass: A techno-economic analysis for a large scale Carbon Capture and Storage (CCS) project in Romania [J].
Cormos, Calin-Cristian .
FUEL, 2016, 169 :50-57
[8]   Waste heat recovery optimization in micro gas turbine applications using advanced humidified gas turbine cycle concepts [J].
De Paepe, Ward ;
Carrero, Marina Montero ;
Bram, Svend ;
Contino, Francesco ;
Parente, Alessandro .
APPLIED ENERGY, 2017, 207 :218-229
[9]   Carbon dioxide utilisation for production of transport fuels: process and economic analysis [J].
Dimitriou, Ioanna ;
Garcia-Gutierrez, Pelayo ;
Elder, Rachael H. ;
Cuellar-Franca, Rosa M. ;
Azapagic, Adisa ;
Allen, Ray W. K. .
ENERGY & ENVIRONMENTAL SCIENCE, 2015, 8 (06) :1775-1789
[10]  
Esposito E, 2019, ENERG ENVIRON SCI, V12, P281, DOI [10.1039/c8ee02897d, 10.1039/C8EE02897D]