Investigation of thermodynamic performances of particle/supercritical CO2 2 fluidized bed heat exchanger integrated with supercritical CO2 2 recompression Brayton cycle for concentrated solar power

被引:8
作者
Cu, Wenkai [1 ]
Fang, Jiabin [1 ]
Guo, Xiaodie [1 ]
Wei, Jinjia [1 ]
Zheng, Nan [1 ]
Chen, Kang [2 ]
Zhou, Zhi [2 ]
机构
[1] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, Xian 710049, Shaanxi, Peoples R China
[2] Northwest Engn Corp Ltd, Xian 710065, Shaanxi, Peoples R China
关键词
Supercritical carbon dioxide; Recompression Brayton cycle; Fluidized bed heat exchanger; Concentrated solar power; DENSE SUSPENSION; ENERGY; PLANTS; PARTICLES; DESIGN; FLOW;
D O I
10.1016/j.enconman.2024.118805
中图分类号
O414.1 [热力学];
学科分类号
摘要
The supercritical carbon dioxide (sCO2) 2 ) Brayton cycle is gaining momentum as a potential alternative for power generation in concentrated solar power plants. Solid particles can be a suitable heat transfer and energy storage medium to achieve high temperatures exceeding 1000 degree celsius . However, the research on concentrated solar power systems that utilize solid particle/sCO2 2 fluidized bed heat exchanger to drive high-performance power cycles is limited. This study presents a comprehensive model of a concentrated solar power system that integrating a sCO2 2 recompression Brayton cycle and a particle/sCO2 2 fluidized bed heat exchanger. Sensitivity analysis investigates the effects of various parameters such as the number of tubes, particle diameter, fluidization air inlet temperature, and fluidization air velocity on the performance of the fluidized bed heat exchanger. Furthermore, thermodynamic analysis and economic assessment are performed on the integrated system. Results indicate that the overall thermal efficiency of the system increases with the turbine inlet temperature, decreases with the main compressor inlet temperature, and reaches a peak value of 0.35 with increasing recompression fraction. The thermal efficiency of the fluidized bed heat exchanger is 99.1 %, the power cycle efficiency is 50.5 %, and the overall thermal efficiency of the system is 32.2 %. These research findings provide a promising alternative for the efficient utilization of solar energy.
引用
收藏
页数:16
相关论文
共 51 条
[1]   Hybrid solar desalination systems driven by parabolic trough and parabolic dish CSP technologies: Technology categorization, thermodynamic performance and economical assessment [J].
Aboelmaaref, Moustafa M. ;
Zayed, Mohamed E. ;
Zhao, Jun ;
Li, Wenjia ;
Askalany, Ahmed A. ;
Ahmed, M. Salem ;
Ali, Ehab S. .
ENERGY CONVERSION AND MANAGEMENT, 2020, 220
[2]   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
[3]   Performance comparison of different supercritical carbon dioxide Brayton cycles integrated with a solar power tower [J].
Al-Sulaiman, Fahad A. ;
Atif, Maimoon .
ENERGY, 2015, 82 :61-71
[4]   Heat Transfer Models of Moving Packed-Bed Particle-to-sCO2 Heat Exchangers [J].
Albrecht, Kevin J. ;
Ho, Clifford K. .
JOURNAL OF SOLAR ENERGY ENGINEERING-TRANSACTIONS OF THE ASME, 2019, 141 (03)
[5]  
[Anonymous], 2021, Version M. 9.11. 0 (R2021b)
[6]   Latest developments, assessments and research trends for next generation of concentrated solar power plants using liquid heat transfer fluids [J].
Arias, I. ;
Cardemil, J. ;
Zarza, E. ;
Valenzuela, L. ;
Escobar, R. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2022, 168
[7]   HEAT-TRANSFER TO OBJECTS IMMERSED IN FLUIDIZED-BEDS [J].
BASKAKOV, AP ;
BERG, BV ;
VITT, OK ;
FILIPPOV.NF ;
KIRAKOSY.VA ;
GOLDOBIN, JM ;
MASKAEV, VK .
POWDER TECHNOLOGY, 1973, 8 (5-6) :273-282
[8]   Heat transfer characteristic in an external heat exchanger with horizontal tube bundle [J].
Blaszczuk, Artur ;
Jagodzik, Szymon .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2020, 149
[9]   EXPERIMENTAL HYDRODYNAMIC STUDY OF GAS-PARTICLE DENSE SUSPENSION UPWARD FLOW FOR APPLICATION AS NEW HEAT TRANSFER AND STORAGE FLUID [J].
Boissiere, Benjamin ;
Ansart, Renaud ;
Gauthier, Daniel ;
Flamant, Gilles ;
Hemati, Mehrdji .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2015, 93 (02) :317-330
[10]  
Brown G.O., 2012, P ASCE CIV ENG C EXP, P34, DOI [DOI 10.1061/40650(2003)4, 10.1061/40650%282003%294, 10.1061/40650(2003)4]