Comparison of Heat Transfer and Pressure Drop Characteristics of Heat Exchangers Having Plain Fins Under Dry and Wet Conditions

  • Kim Nae-Hyun (Department of Mechanical Engineering, University of lncheon) ;
  • Sin Tae-Ryong (Graduate School, University of lncheon, lncheon) ;
  • Lee Eung-Ryul (Graduate School, University of lncheon, lncheon)
  • Published : 2005.09.01

Abstract

In this study, dry and wet surface pressure drop and heat transfer characteristics of heat exchangers having plain fins were investigated. Nine samples having different fin pitches and rows were tested. The wet surface heat transfer coefficient was reduced from experimental data using enthalpy-potential method. The wet surface heat transfer coefficients were approximately equal to the dry surface values except for one row configuration. For one row configuration, the wet surface heat transfer coefficients were approximately $30\%$ lower than the dry surface values. For the pressure drop, the wet surface yielded approximately $30\%$ higher values compared with the dry surface counterpart. Data were compared with existing correlations.

Keywords

References

  1. Kim, N.-H., Oh, W.-K., Cho, J.-P., Park, W. -Y and Baek, Y, 2003, Data reduction on the air-side heat transfer coefficients of heat exchangers under dehumidifying conditions, Korean Journal of Air-Conditioning and Refrigeration, Vol. 15, No. 1, pp. 73-85
  2. ARI 410-81, Standard for forced-circulation air-cooling and air-heating coils, American Refrigeration Institute
  3. McQuiston, F. C., 1975, Fin efficiency with combined heat and mass transfer, ASHRAE Trans., Vol. 81, No. 1, pp. 350-355
  4. McQuiston, F. C., 1978, Heat, mass and momentum transfer data for five plate-fin-tube surfaces, ASHRAE Trans., Vol. 84, Part 1, pp. 266-293
  5. Wang, C.-C., Hsieh, Y.-C. and Lin, Y.-T., 1997, Performance of plate finned tube heat exchangers under dehumidifying conditions, J. Heat Transfer, Vol. 119, pp. 109-117 https://doi.org/10.1115/1.2824075
  6. Eckels, P. W. and Rabas, T.J., 1987, Dehumidification: on the correlation of wet and dry transport process in plate finned-tube heat exchangers, J. Heat Transfer, Vol. 109, pp. 575-582 https://doi.org/10.1115/1.3248127
  7. Mirth, D. R., Ramadhyani, S. and Hittle, D. C., 1993, Thermal performance of chilled water cooling coils at low water velocities, ASHRAE Trans., Vol. 99, Pt. 1, pp. 43-53
  8. Hong, K. and Webb, R. L., 1999, Performance of dehumidifying heat exchangers with and without wetting coatings, J. Heat Transfer, Vol. 121, pp. 1018-1026 https://doi.org/10.1115/1.2826052
  9. Kim, N.-H., Kim, J.-S., Yun, J.-H., Peck, J.-H., Lee, S.-K., Nam, S.-B. and Kwon, H.-J., 1997, Wet surface performance test of fin-and-tube heat exchangers with slit-wavy fin, Korean Journal of Air-Conditioning and Refrigeration, Vol. 9, No. 2, pp. 153-162
  10. Wang, C.-C., Chi, K.-Y. and Chang, C.-J., 2000, Heat transfer and friction characteristics of plain fin-and-tube heat exchangers, Part II: correlation, Int. J. Heat Mass Trans., Vol. 43, pp. 2693-2700 https://doi.org/10.1016/S0017-9310(99)00333-6
  11. Kim, N.-H., Youn, B. and Webb, R. L., 1999, Air-side heat transfer and friction correlations for plain fin-and-tube heat exchangers with staggered tube arrangements, J. Heat Transfer, Vol. 121, pp. 662-667 https://doi.org/10.1115/1.2826030
  12. Gray, D. L. and Webb, R. L., 1986, Heat transfer and friction correlations for plate fin-and-tube heat exchangers having plain fins, Proceedings of the 9th International Heat Transfer Conference, Taylor & Francis, London, San Francisco, pp. 2745-2750
  13. McQuiston, F. C., 1978, Correlation of heat, mass and momentum transport coefficients for plate-fin-tube heat transfer surfaces with staggered tubes, ASHRAE Transactions, Part 1, Vol. 84, pp. 294-309
  14. Wang, C.-C., Hsieh, Y.-C. and Lin, Y.-T., 1997, Performance of plate finned tube heat exchangers under dehumidifying conditions, J. of Heat Transfer, Vol. 119, pp. 109-117 https://doi.org/10.1115/1.2824075
  15. ASHRAE Standard 41.1, 1986, Standard method for temperature measurement, ASHRAE
  16. ASHRAE Standard 41.2, 1986, Standard method for laboratory air-flow measurement, ASHRAE
  17. ASHRAE Standard 41.5, 1986, Standard measurement guide, engineering analysis of experimental data, ASHRAE
  18. Taborek, J., 1998, F and $\theta$ charts for crossflow arrangements, in Heat Transfer Enhancement of Heat Exchangers, Eds., S. Kakac, A. E. Bergles, F. Mayinger and H. Yuncu, Kluwer Academic Press, pp. 141-162
  19. Gnielinski, V., 1976, New equations for heat and mass transfer in turbulent pipe flows, Int. Chem. Eng., Vol. 16, pp. 359-368
  20. Schmidt, T. E., 1949, Heat trasfer calculations for extended surfaces, J. ASRE, Refrigeration Engineering, Vol. 4, pp. 351-357
  21. Rich, D. G., 1973, The effect of fin spacing on the heat transfer and friction preformance of multi-row, plate fin-and-tube heat exchangers, ASHRAE Transactions, Part 2, Vol. 79, pp. 137-145
  22. Rich, D. G., 1975, The effect of number of tube rows on the heat transfer performance of smooth plate-fin-tube heat exchangers, ASHRAE Trans., Vol. 81, Part 1, pp. 307-317
  23. Idem, S. A., Jacobi, A. M. and Goldschmidt, V. W., 1990, Heat transfer characterization of a finned-tube heat exchanger (with and without condensation), Journal of Heat Transfer, Vol. 112, pp. 64-70 https://doi.org/10.1115/1.2910366