An Experimental Study on Convective Boiling of R-22 and R-410A in Horizontal Smooth and Micro-fin Tubes

  • Kim, Yongchan (Department of Mechanical Engineering, Korea University) ;
  • Seo, Kook-Jeong (Department of Mechanical Engineering, Korea University) ;
  • Lee, Kyu-Jung (Department of Mechanical Engineering, Korea University) ;
  • Park, Youn cheol (Department of Mechanical Engineering, Korea University)
  • Published : 2001.08.01

Abstract

Evaporation heat transfer coefficients and pressure drops were measured for smooth and micro-fin tubes with R-22 and R-410A. Heat transfer measurements were performed for 3.0m long horizontal tubes with nominal outside diameters of 9.52 and 7.0mm over an evaporating temperature range of -15 to 5$\^{C}$, a mass flux range of 68 to 211kg/㎡s, and a heat flux range of 5 to 15kW/㎡. It was observed that the heat transfer coefficient increased with mass flux. Evaporation heat transfer coefficients of R-22 and R-410A increased as the evaporating temperature dropped at a lower heat flux. Generally, R-420A showed the higher heat transfer coefficients than R-22 in the range of low mass flux, high heat flux and high evaporating temperature. Pressure drop increased with a decrease of evaporating temperature and a rise of mass flux. Pressure drop of R-22 was higher than that of R-410A at the same mass flux.

Keywords

References

  1. Chen, J.C., 1966, 'Correlation for Boiling Heat Transfer to Saturated Fluids in Convective Flow,' I & EC Process Design and Development, Vol. 5, No. 3, pp. 322-329 https://doi.org/10.1021/i260019a023
  2. Ha, S. C., 2000, 'Some Aspects of Experimental In-Tube Evaporation,' KSME International Journal, Vol. 14, NO. 5, pp. 537-546
  3. Klimenko, V. V., 1988, 'A Generalized Correlation for Two-Phase Forced Flow Heat Transfer,' International Journal of Heat and Mass Transfer, Vol. 31, No. 3, pp. 541-552 https://doi.org/10.1016/0017-9310(88)90035-X
  4. Kline, S. J. and McClintock, F. A., 1953, 'Describing Uncertainties Single Sample Experiments,' Mechanical Engineering, Vol. 75, pp. 3-8
  5. Kuo, C. S. and Wang, C. C., 1996, 'In-tube evaporation of HCFC-22 in a 9.52 mm micro-fin/smooth tube,' Vol. 39, No. 12, pp. 2559-2569 https://doi.org/10.1016/0017-9310(95)00326-6
  6. Kuo, C. S., Wang, C. C., Cheng, W. Y. and Lu, D. C., 1995, 'Evaporation of R-22 in a 7mm Micro-fin Tube,' ASHRAE Transactions, Vol. 95, pp. 1055-1061
  7. Kwak, K. M. and Bai, C. H., 'A Discussion to the Heat Transfer of Microfin Tube by Fin Geometry,' Proceeding of SAREK Summer Meeting, pp. 897-902
  8. Schlager, L. M., Pate, M. B. and Bergles,A. E., 1990, 'Evaporation and Condensation Heat Transfer and Pressure Drop in Horizontal,12.7mm Micro-fin Tube with Refrigerant 22,' Transactions of the ASME Journal of Heat Transfer, Vol. 112, Nov., pp. 1041-1047
  9. Wang, C. C., Kuo, C. S., Chang, Y. J. and Lu, D. C., 1996, 'Two Phase Flow Heat Transfer and Friction Characteristics of R-22 and R-407c,' ASHRAE Transactions, Vol. 96, pp. 830-838
  10. Wijaya, H. and Spatz, M. W., 1995, 'Two Phase Flow Heat Transfer and Pressure Drop Characteristics of R-22 and R-32/125, ' ASHRAE Transactions, Vol. 101, pp. 1020-1027