Experimental Study on S-CO2 Forced Convection Heat Transfer in Tubes under High-temperature Condition

被引:0
|
作者
Xie R. [1 ]
Zhang G. [1 ]
Zhao D. [1 ]
Lu G. [1 ]
Hong G. [1 ,2 ]
Zhang Y. [1 ,2 ]
机构
[1] College of Energy, Xiamen University, Xiamen
[2] Fujian Research Center for Nuclear Engineering, Xiamen
关键词
buoyancy effect; empirical correlation; high-temperature condition; supercritical carbon dioxide; thermal acceleration effect;
D O I
10.7538/yzk.2023.youxian.0248
中图分类号
学科分类号
摘要
Under high-temperature conditions, supercritical carbon dioxide (S-CO2) power conversion systems have significant advantages, which show great potential in improving energy utilization efficiency, reducing environmental pollution, and realizing sustainable energy development. S-CO2, as a high-efficiency working fluid, can achieve high efficiency in higher temperature thermodynamic cycles, which helps to reduce fuel consumption and greenhouse gas emissions. Since the S-CO2 power cycle is significant to energy conversion and utilization, many researchers have conducted experimental studies on the convective heat transfer characteristics of S-CO2. However, existing studies mainly focus on low-temperature condition (10-200 ℃), and experimental data under high-temperature condition (200-500 ℃) are scarce. Most of the research conditions on the heat transfer characteristics of S-CO2 have not reached the optimal temperature range of the S-CO2 power conversion system, in order to master the critical data of the relevant design, it is necessary to carry out experimental research on the heat transfer characteristics of S-CO2 under high heat flux conditions, which holds a crucial significance in the development of associated power conversion systems. This paper first introduced the construction process of the S-CO2 forced circulation test bench, and evaluated the uncertainty of the relevant experimental data. The main temperature range of the experiment is 450-800 K, the pressure range is 7.40-10.22 MPa, and the heat flux range is 20-1 000 kW/m2. The heat transfer characteristics of S-CO2 in a vertical tube under high-temperature conditions were studied experimentally, and the effects of thermal acceleration and buoyancy on heat transfer were analyzed. The results show that the heat transfer trend of S-CO2 is similar to that of gaseous CO2 under high-temperature conditions, but the values are quite different, and the influence of thermal acceleration and buoyancy effect on the heat transfer of high-temperature S-CO2 is negligible. Finally, in order to develop a reliable prediction method of S-CO2 convection heat transfer under high-temperature conditions, this paper collected the empirical correlations of S-CO2 heat transfer in vertical heating circular tubes commonly found in the literature, and analyzed them under high heat flux, evaluated and analyzed their experimental prediction high-temperature conditions. It is found that there are some differences with the existing experimental data. Therefore, this paper proposes an empirical correlation suitable for high-temperature S-CO2 heat transfer. The newly proposed heat transfer correlation has the highest calculation accuracy, which calculates 96.65% of experimental data within ±10% error. It can achieve higher accuracy, which meets the actual engineering needs. © 2023 Atomic Energy Press. All rights reserved.
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页码:1761 / 1770
页数:9
相关论文
共 18 条
  • [1] LIN S, SEFIANE K, CHRISTY J., Prospects of confined flow boiling in thermal management of microsystems, Applied Thermal Engineering, 22, 7, pp. 825-837, (2002)
  • [2] FRONK B M, RATTNER A S., High-flux thermal management with supercritical fluids, Journal of Heat Transfer, 138, 12, pp. 501-504, (2016)
  • [3] PIORO I L, DUFFEY R B., Experimental heat transfer in supercritical water flowing inside channels (survey), Nuclear Engineering and Design, 235, 22, pp. 2407-2430, (2005)
  • [4] RAO N T, OUMER A N, JAMALUDIN U K., State-of-the-art on flow and heat transfer characteristics of supercritical CO2 in various channels, Journal of Supercritical Fluids, 116, pp. 132-147, (2016)
  • [5] CABEZA L F, GRACIA A D, FERNANDEZ A I, Et al., Supercritical CO2 as heat transfer fluid: A review, Applied Thermal Engineering, 125, pp. 799-810, (2017)
  • [6] EHSAN M M, GUAN Z, KLIMENKO A Y., A comprehensive review on heat transfer and pressure drop characteristics and correlations with supercritical CO2 under heating and cooling applications, Renewable & Sustainable Energy Reviews, 92, 9, pp. 658-675, (2018)
  • [7] XIE J, LIU D, YAN H, Et al., A review of heat transfer deterioration of supercritical carbon dioxide flowing in vertical tubes: Heat transfer behaviors, identification methods, critical heat fluxes, and heat transfer correlations, International Journal of Heat and Mass Transfer, 149, pp. 210-233, (2020)
  • [8] McELIGOT D M, COON C W, PERKINS H C., Relaminarization in tubes, International Journal of Heat and Mass Transfer, 13, 2, pp. 431-433, (1970)
  • [9] KURGANOV V A, KAPTIL″NY A G., Velocity and enthalpy fields and eddy diffusivities in a heated supercritical fluid flow, Experimental Thermal & Fluid Science, 5, 4, pp. 465-478, (1992)
  • [10] JACKSON J D., Fluid flow and convective heat transfer to fluids at supercritical pressure, Nuclear Engineering and Design, 264, 11, pp. 24-40, (2013)