Advanced exergy analysis of the combined S-CO2/ORC system

被引:49
作者
Fallah, M. [1 ,2 ]
Mohammadi, Z. [3 ]
Mahmoudi, S. M. Seyed [3 ]
机构
[1] Azarbaijan Shahid Madani Univ, Dept Mech Engn, Tabriz, Iran
[2] Azarbaijan Shahid Madani Univ, Res Inst Appl Power Syst Studies, Tabriz, Iran
[3] Univ Tabriz, Dept Mech Engn, Tabriz, Iran
关键词
Advanced exergy analysis; Conventional exergy; Combined cycle; Low or high temperature recuperator; CO2 BRAYTON CYCLES; CARBON-DIOXIDE; OPTIMIZATION; PERFORMANCE; WASTE; AIR;
D O I
10.1016/j.energy.2021.122870
中图分类号
O414.1 [热力学];
学科分类号
摘要
The real origin of irreversibility and improvement possibility of the combined super critical carbon dioxide and organic Rankine cycle (S-CO2/ORC) are investigated based on the advanced exergy analysis. The interaction between topping and bottoming cycles is investigated, for the first time in literature, in addition to the evaluation of interaction among system components. The results show that 34.76% of the overall exergy destruction rate is avoidable, and can be reduced. Also, 61.40% of the avoidable part is endogenous, which can be decreased by modifying the components themselves. Based on the avoidable endogenous part of exergy destruction, the high temperature recuperator, turbine1 and pre-cooler1 have the higher order of improvement priority, respectively. The results also indicate that the major part of inefficiency occurring in the reactor, compressor1 and low temperature recuperator is due to the high temperature recuperator. Another noteworthy result is that 75.4% of the overall exergy destruction occurring in the ORC is emanated from irreversibilities in the S-CO2 cycle and 62.98% of this amount is avoidable. (C) 2021 Published by Elsevier Ltd.
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页数:19
相关论文
共 43 条
[1]   REVIEW OF SUPERCRITICAL CO2 POWER CYCLE TECHNOLOGY AND CURRENT STATUS OF RESEARCH AND DEVELOPMENT [J].
Ahn, Yoonhan ;
Bae, Seong Jun ;
Kim, Minseok ;
Cho, Seong Kuk ;
Baik, Seungjoon ;
Lee, Jeong Ik ;
Cha, Jae Eun .
NUCLEAR ENGINEERING AND TECHNOLOGY, 2015, 47 (06) :647-661
[2]   Thermoeconomic performance and optimization of a novel cogeneration system using carbon dioxide as working fluid [J].
Akbari, A. D. ;
Mahmoudi, S. M. S. .
ENERGY CONVERSION AND MANAGEMENT, 2017, 145 :265-277
[3]   Thermoeconomic analysis & optimization of the combined supercritical CO2 (carbon dioxide) recompression Brayton/organic Rankine cycle [J].
Akbari, Ata D. ;
Mahmoudi, Seyed M. S. .
ENERGY, 2014, 78 :501-512
[4]   CARBON DIOXIDE CONDENSATION CYCLES FOR POWER PRODUCTION [J].
ANGELINO, G .
JOURNAL OF ENGINEERING FOR POWER, 1968, 90 (03) :287-&
[5]   Various supercritical carbon dioxide cycle layouts study for molten carbonate fuel cell application [J].
Bae, Seong Jun ;
Ahn, Yoonhan ;
Lee, Jekyoung ;
Lee, Jeong Ik .
JOURNAL OF POWER SOURCES, 2014, 270 :608-618
[6]   Power-based performance comparison between carbon dioxide and R125 transcritical cycles for a low-grade heat source [J].
Baik, Young-Jin ;
Kim, Minsung ;
Chang, Ki Chang ;
Kim, Sung Jin .
APPLIED ENERGY, 2011, 88 (03) :892-898
[7]   Conventional and advanced exergoenvironmental analysis of a steam methane reforming reactor for hydrogen production [J].
Boyano, A. ;
Morosuk, T. ;
Blanco-Marigorta, A. M. ;
Tsatsaronis, G. .
JOURNAL OF CLEANER PRODUCTION, 2012, 20 (01) :152-160
[8]   Conventional and advanced exergy analysis of an ejector refrigeration system [J].
Chen, Jianyong ;
Havtun, Hans ;
Palm, Bjorn .
APPLIED ENERGY, 2015, 144 :139-151
[9]   Supercritical carbon dioxide cycles for power generation: A review [J].
Crespi, Francesco ;
Gavagnin, Giacomo ;
Sanchez, David ;
Martinez, Gonzalo S. .
APPLIED ENERGY, 2017, 195 :152-183
[10]  
Dostal V., 2004, MITANPTR100