Recuperators investigation for high temperature supercritical carbon dioxide power generation cycles

被引:53
作者
Gkountas, Apostolos A. [1 ]
Stamatelos, Anastassios M. [1 ]
Kalfas, Anestis I. [2 ]
机构
[1] Univ Thessaly, Dept Mech Engn, Volos 38334, Greece
[2] Aristotle Univ Thessaloniki, Dept Mech Engn, Thessaloniki 54124, Greece
关键词
Thermodynamic modeling; Supercritical CO2; Recompression cycle; Printed-circuit heat exchangers; Recuperators' analysis; CO2; PERFORMANCE; GAS;
D O I
10.1016/j.applthermaleng.2017.07.092
中图分类号
O414.1 [热力学];
学科分类号
摘要
Supercritical carbon dioxide (s-CO2) Brayton cycles are a promising technology for the next generation power conversion cycles, attaining equivalent or higher cycle efficiency compared to conventional power cycles at similar temperatures (550-750 degrees C). The recompression cycle attracts the main research interest among the s-CO2 layouts. Recompressing a fraction of the flow without heat rejection, results to an increase in thermal efficiency, while the majority of heat transfer occurs in recuperators. In this study, a thermodynamic analysis of a 600 MWth power cycle has been carried out using two different simulation tools to model the recompression system. The analysis focuses on the parameters that have the most significant impact on the components and cycle efficiency. A segmental analysis of the recuperators took place to assess the effect of flow characteristics on the heat transfer. Finally, a comparative analysis of the results of the two simulation tools versus the results of a reference cycle from literature is carried out, showing that the prediction of the overall heat transfer coefficient and recuperator effectiveness between the developed code and reference model has a maximum deviation of 4%, whereas the prediction deviation between the commercial software and reference model is about 2.8%. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1094 / 1102
页数:9
相关论文
共 31 条
  • [1] 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
    Ahmadi, Mohammad H.
    Mehrpooya, Mehdi
    Pourfayaz, Fathollah
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2016, 119 : 422 - 434
  • [2] Design consideration of supercritical CO2 power cycle integral experiment loop
    Ahn, Yoonhan
    Lee, Jekyoung
    Kim, Seong Gu
    Lee, Jeong Ik
    Cha, Jae Eun
    Lee, Si-Woo
    [J]. ENERGY, 2015, 86 : 115 - 127
  • [3] CARBON DIOXIDE CONDENSATION CYCLES FOR POWER PRODUCTION
    ANGELINO, G
    [J]. JOURNAL OF ENGINEERING FOR POWER, 1968, 90 (03): : 287 - &
  • [4] Aspen Plus, 2014, ASP
  • [5] Experimental and numerical investigation of supercritical CO2 test loop transient behavior near the critical point operation
    Bae, Seong Jun
    Ahn, Yoonhan
    Lee, Jekyoung
    Kim, Seong Gu
    Baik, Seungjoon
    Lee, Jeong Ik
    [J]. APPLIED THERMAL ENGINEERING, 2016, 99 : 572 - 582
  • [6] Study on CO2 - water printed circuit heat exchanger performance operating under various CO2 phases for S-CO2 power cycle application
    Baik, Seungjoon
    Kim, Seong Gu
    Lee, Jekyoung
    Lee, Jeong Ik
    [J]. APPLIED THERMAL ENGINEERING, 2017, 113 : 1536 - 1546
  • [7] Parametric study and optimization of a transcritical power cycle using a low temperature source
    Cayer, Emmanuel
    Galanis, Nicolas
    Nesreddine, Hakim
    [J]. APPLIED ENERGY, 2010, 87 (04) : 1349 - 1357
  • [8] Alternative cycles based on carbon dioxide for central receiver solar power plants
    Chacartegui, R.
    Munoz de Escalona, J. M.
    Sanchez, D.
    Monje, B.
    Sanchez, T.
    [J]. APPLIED THERMAL ENGINEERING, 2011, 31 (05) : 872 - 879
  • [9] Chang H. Oh, 2009, J ENG GAS TURB POWER, V132
  • [10] Pressure drop and heat transfer characteristics of a high-temperature printed circuit heat exchanger
    Chen, Minghui
    Sun, Xiaodong
    Christensen, Richard N.
    Skavdahl, Isaac
    Utgikar, Vivek
    Sabharwall, Piyush
    [J]. APPLIED THERMAL ENGINEERING, 2016, 108 : 1409 - 1417