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Experimental Study on the Air-Side Heat Transfer Characteristics of a Spirally-Coiled Circular Fin-Tube Heat Exchanger According to Geometric Parameters

형상변수에 따른 나선형 원형핀-튜브 열교환기의 공기측 열전달 특성에 관한 실험적 연구

  • Received : 2009.12.28
  • Accepted : 2010.02.24
  • Published : 2010.05.01

Abstract

The objective of this study is to investigate the air-side heat transfer characteristics of a spirally-coiled circular fin-tube heat exchanger for various geometric parameters under non-frosting conditions. The heat transfer characteristics of the heat exchanger were analyzed with respect to heat exchanger geometries, and then, the characteristics were compared with those of rectangular-plate fin-tube heat exchangers with discrete fins. The heat transfer coefficient increased with a decrease in the number of tube rows and an increase in the fin pitch. The optimum length of the L-foot was 2.7 mm. In addition, the heat transfer rate increased with a decrease in the tube pitch and the tube thickness. The heat transfer coefficient of the spirally-coiled circular fin-tube heat exchanger was 24.3% higher than that of the rectangular-plate fin-tube heat exchanger.

본 연구의 목적은 무착상 조건에서 나선형 원형핀-튜브 열교환기의 형상변수에 따른 열전달특성을 고찰하고 평판 사각핀-튜브 열교환기와 열전달성능을 비교하는 것이다. 나선형 원형핀-튜브 열교환기는 Lfoot 길이 2.7 mm 에서 열전달계수가 최대로 나타났으며, 공기측 열전달계수는 튜브열수가 2 열에서 5 열로 증가하면서 평균 10% 감소하였고 핀피치가 5 mm 에서 10 mm 로 증가하면서 평균 17.5% 증가하였다. 모든 풍량조건에서 나선형 원형핀-튜브 열교환기의 튜브피치 30 mm 가 35 mm 보다 열전달량이 평균 5.1% 높게 나타났고 튜브두께 0.5 mm 가 0.7 mm 보다 열전달량이 평균 4.1% 높게 나타났다. 나선형 원형핀-튜브 열교환기의 열전달계수가 평판 사각핀-튜브 열교환기에 비하여 평균 24.3% 정도 높게 나타났다.

Keywords

References

  1. Lee, M. Y., Kim, S. O. and Kim, Y., 2007, "Performance Evaluations of a Residential Small Multi-Refrigeration System Considering the Adiabatic Characteristics," Trans. of the KSME, Vol. 31, No. 10, pp. 868-875.
  2. Lee, M. Y. and Kim, S. O., 2005, "A Study on the Performance of a Domestic Small Multi Refrigerator According to a Capillary Tube Change," Trans. of the KSME, Vol. 29, No. 6, pp. 763-771.
  3. Mon, M. S. and Gross, U., 2004, "Numerical Study of Fin-spacing Effects in Annular-finned Tube Heat Exchangers," Int. J. Heat Mass Transfer, Vol. 47, pp. 1953-1964. https://doi.org/10.1016/j.ijheatmasstransfer.2003.09.034
  4. Yun, R., Kim, Y., Kim, S. and Choi, J. M., 2005, "Experimental Study on the Heat Transfer Characteristics of Spiral Fin-tube Heat Exchanger," Trans. of the SAREK, Vol. 17, No. 6, pp. 529-535.
  5. Kim, Y. H. and Kim, Y., 2005, "Heat Transfer Characteristics of Flat Plate Finned-tube Heat Exchangers with Large Fin Pitch," Int. J. of Refrigeration, Vol. 28, pp. 851-858. https://doi.org/10.1016/j.ijrefrig.2005.01.013
  6. ASHRAE Guideline 2, 1986, "Engineering Analysis of Experimental Data," ASHRAE, Atlanta, USA.
  7. Incropera, F. P. and Dewitt, D. P., 2006, "Fundamentals of Heat and Mass Transfer," 5th edition, Wiley, New York, 466-499.
  8. Gnielinski, V., 1976, "New Equation for Heat and Mass Transfer in Turbulent Pipe and Channel Flow," Int. Chem. Eng. Vol. 16, 359-368.
  9. Lee, M. Y., Kang, T. H. and Kim, Y., 2009, "Air-side Heat Transfer Characteristics of Spiral-type Circular Fin-tube Heat Exchangers," Int. J. of Refrigeration, Vol. 33, pp. 313-320.
  10. Mon, M. S., 2003, "Numerical Study of Air-side Heat Transfer and Pressure Drop in Circular Finnedtube Heat Exchangers," Ph.D. Thesis, Freiberg Technischen University.
  11. Kim, Y. H., 2004, "Study on the Frosting and Defrosting Performance of Fin-tube Heat Exchangers," Ph. D. Thesis, Korea University.
  12. Incropera, F. P. and Dewitt, D. P., 2002, "Fundamentals of Heat and Mass Transfer," John Wiley & Sons, 4th edition, pp. 88-182, 326-431.

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