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Forced Convection Heat Transfer for Two Circular Tube Arrays with Annular Fins

환형휜이 부착된 두 개의 원형관 배열에 대한 강제대류 열전달

  • Kim, Seung-iI (Dept. of mechanical engineering, Kumoh National Institute of Technology) ;
  • Park, Sang-Hee (Dept. of mechanical engineering, Kumoh National Institute of Technology)
  • 김승일 (금오공과대학교 기계공학과 대학원) ;
  • 박상희 (금오공과대학교 기계공학과)
  • Received : 2020.11.22
  • Accepted : 2020.12.11
  • Published : 2020.12.31

Abstract

This study was carried out numerically to investigate the air flow and thermal performance around single and parallel fin-tube heat exchangers and the cooling performance of the fluid inside the heat exchangers. In this study, the air velocity(1~7m/s), the pitch of fin(4, 6.1, 8, 11.3, 18.3, 44mm) and the diameter of fin(31, 33, 35, 37, 39mm) were varied. The flow rate of the water at the fin-tube heat exchanger inlet is 89cc/min and the water temperature is 353K. The air temperature at the upstream region of the heat exchanger is 300K. flow rate of the water at the fin-tube heat exchanger inlet is 80cc/min and the water temperature is 353K. It was found that the air pressure drop around single and parallel fin-tube heat exchangers was highly dependent on the air velocity and the fin pitch, but was independent of the fin diameter. Also, it was shown that pressure drop increased more the parallel arrangements than in single heat exchanger. The temperature difference of water at the inlet and outlet of the heat exchanger depended on the air velocity, the fin pitch and the fin diameter, and it was found that the parallel arrangement method further reduced the temperature of water. It was shown that the Nusselt number increased as the Reynolds number and the fin pitch increased, and decreased as the fin diameter increased.

Keywords

References

  1. W. M. Kays and A. L. London, "Compact Heat Exchanger", McGraw-Hill, U.S.A., pp.220-224. (1964).
  2. D. T. Beecher and T. J. Fagan, "Effects of fin pattern on the air side heat transfer coefficient in plate finned tube heat exchangers" Presented at the American Society of Heating, (1987).
  3. J. Stasiulevicius, A. Skrinska, A. Zukau-sskas and G. F. Hewitt, "Heat Transfer of Finned Tube Bundl es in Crossflow", Hemisphere Publishing Co., New York, U.S.A., pp.50-74.(1988).
  4. K. S. Lee and J. Y. Yun, "Heat Trans fer Characteristics of Fin and Tube Heat Exchangers with Various Interrupted Surfaces for Air Conditioning Application" KSME International Journal, Vol. 20, No. 12, pp.3938-3948, (1996).
  5. H. C. Kang, M. H. Kim and D. Y. Cho, "Heat Transfer Coefficient of a Single Circular Fin-Tube Heat Exchanger", Proc. of Korean J. of Air-Conditioning and Refrigeration Eng., Vol. 1, pp. 460-465. (2001).
  6. M. S., Mon and U., Gross, "Numerical study of fin-spacing effects in annular-finned tube heat exchangers", Int. J. Heat and Mass Transfer 47, 1953-1964, (2004). https://doi.org/10.1016/j.ijheatmasstransfer.2003.09.034
  7. H. C. Kang and M. C. Kang, "Forced convection correlation for single circular fin-tube heat exchanger", Korean J. of Air-Conditioning and Refrigeration Eng., Vol. 16, No. 6, pp. 584-589. (2004).
  8. B. Sahin, A. Akkoca, N. A. and H. Akilli, "Investigations of flow characteristics in a plate fin and tube heat exchanger model composed of single cylinder" Int. J. Heat and Fluid Flow, Vol. 27, pp.522-530, (2006) https://doi.org/10.1016/j.ijheatfluidflow.2005.11.005
  9. H. T. Chen and W. L. Hsu, "Estimation of heat-transfer characteristics on a vertical annular circular fin of finned-tube heat exchangers in forced convection", Int. J. Heat and Mass Transfer 51, pp.1920-1932, (2008). https://doi.org/10.1016/j.ijheatmasstransfer.2007.06.035
  10. J. H. Lee, M. G. Lim and H. C. Kang, "Forced convection characteristics of V shape circular fin-tube heat exchanger", Korean J. of Air-Conditioning and Refrigeration Eng., Vol. 21, No. 12, pp.649-655. (2009).