Modeling of Pressure Drop for Water Vapor Flow across Tube Banks inside Horizontal Tube Absorber

  • Phan Thanh Tong (Graduate School, Department of Refrigeration and Air-conditioning Engineering, Pukyong National University) ;
  • Yoon Jung-In (School of Mechanical Engineering, Pukyong National University) ;
  • Kim Eun-Pil (School of Mechanical Engineering, Pukyong National University)
  • 발행 : 2006.05.01

초록

A model for a pressure drop of water vapor flow across tube banks in a horizontal tube absorber of an absorption chiller/heater using LiBr solution as a working fluid has been developed based on a commercial 20RT(70kW) absorption chiller/heater. The numerical results show that the characteristic of the pressure drop in the shell side of the horizontal tube absorber is completely different from that in a conventional shell and tube heat exchanger. Especially, solution film thickness has significant influence on the vapor pressure drop in the horizontal tube absorber. In addition, the effects by the tube diameters, the longitudinal pitch to diameter ratio, and Reynolds number of the vapor flow, on the vapor pressure drop have been studied to evaluate the compactness of tube absorber. It was found that the vapor pressure drop decreases as tube diameter increases, the longitudinal pitch to diameter ratio increases, and Reynolds number of the vapor flow decreases. A comparison of the present study results with well-established experimental and numerical results showed a good overall agreement.

키워드

참고문헌

  1. G. Grossman, 'Simultaneous heat and mass transfer in film absorption under laminar flow', International Journal of Heat and Mass Transfer, Vol. 26, No. 3, pp. 357-371, 1983 https://doi.org/10.1016/0017-9310(83)90040-6
  2. T. Nishimura, 'Flow across tube banks', Encyclopedia of Fluid Mechanics, Vol. 1, pp. 763-785, 1986
  3. F. Zdravistch, C. A. Fletcher, M. Behnia, 'Numerical laminar and turbulent fluid flow and heat transfer predictions in tube banks', International Journal of Numerical Method for Heat and Fluid Flow, Vol. 5, pp. 717-733, 1995 https://doi.org/10.1108/EUM0000000004086
  4. Y. O. Wang, L. A. Penner, S. J. Ormiston, 'Analysis of laminar forced convection of air or crossflow in banks of staggered tubes', Numerical Heat Transfer, Part A, Vol. 38, pp. 819-845, 2000 https://doi.org/10.1080/104077800457449
  5. A. S. Wilson, M. K. Bassiouny, 'Modeling of heat transfer for flow across tube banks', Chemical Engineering and Processing, Vol. 39, pp. 1-14, 2000 https://doi.org/10.1016/S0255-2701(99)00069-0
  6. H. Suzuki, W. Nagamoto, T. Sugiyama, 'Simulation on vapor flow in the absorber/evaporator of an absorption chiller', Transactions of the JSRAE, Vol. 20, No. 3, pp. 325-331, 2003
  7. Y. A. Çengel, Heat Transfer, A Practical Approach, The McGraw-Hill Companies, Inc., 1998
  8. S. V. Partankar, C. H. Liu, and E. M. Sparrow, 'Fully develop flow and heat transfer in ducts having streamwiseperiodic variations of cross-sectional area', Journal of Heat Transfer, Vol. 99, pp. 180-186, 1977 https://doi.org/10.1115/1.3450666
  9. FLUENT 5 User's Guide, Fluent Incorporated, 1998
  10. S. V. Partankar, 'Numerical heat transfer and fluid flow', Hemisphere Publishing Co., Washington, D.C., 1980
  11. T. Nishimura, Y. Kawamura, 'Analysis of flow across tube banks in low Reynolds number region', Journal of Chemical Engineering of Japan, Vol. 14, pp. 267-272, 1981 https://doi.org/10.1252/jcej.14.267