Skip to main content
Log in

Performance of heat transfer and pressure drop in a spirally indented tube

  • Published:
KSME International Journal Aims and scope Submit manuscript

Abstract

In an effort to develop a heat transfer enhancement technique for low temperature applications such as utilization of LNG cold energy, an experiment was carried out to evaluate the heat transfer and the pressure drop performance for a spirally indented tube using ethylene-glycol and water solutions and pure water under horizontal single-phase conditions. The test tube diameter was 14.86 mm and the tube length was 5.38 m. Heat transfer coefficients and friction factors for both inner and outer surfaces of the test tube were calculated from measurements of temperatures, flowrates and pressure drops. Correlations of heat transfer coefficients in the spirally indented tube, which were applicable for laminar and turbulent regimes were proposed for inner, and outer surfaces. The correlations showed that heat transfer coefficients for the spirally indented tube were much higher than those for smooth tubes, increased by more than 8 times depending upon the Reynolds number. The correlations were compared with other correlations for various types of surface roughness. The effect of the Prandtl number on the heat transfer characteristics was discussed. The critical Reynolds number from the laminar flow to the turbulent flow inside the spirally indented tube was found to be around Re=1,000.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

Abbreviations

C pn :

Specific heat of hot fluid

D i :

Inside tube diameter

D o :

Outside tube diameter

f :

Darcy friction factor

G h :

Mass flow rate of hot fluid

h :

Heat transfer coefficient

k w :

Tube wall thermal conductivity

Pr :

Prandtl number

Q :

Heat transfer rate

Re :

Reynolds number

T pf :

Mean cold fluid temperature

T hf :

Mean hot fluid temperature

T hf, i :

Mean inlet hot fluid temperature

T hf, w :

Mean outlet hot fluid temperature

T w :

Average wall temperature

References

  • Berger, F. P. and Hau, F. L., 1979, “Local Mass/Heat Transfer Distribution on Surfaces Roughened with Small Square Ribs,”Int. J. Heat Mass Transfer, Vol. 22, pp. 1645–1656.

    Article  Google Scholar 

  • Blumenkrantz, A. and Taborek, J., 1971, “Heat Transfer and Pressure Drop Characteristics of Turbotec Spirally Deep Grooved Tubes in the Laminar and Transition Regime,” Report 2439-300-8, Heat Transfer Research, Inc.

  • Dittus, F. W. and Boelter, L. M. K., 1930, Univ. Calif. Pubs. Eng., Vol. 2, p. 443.

    Google Scholar 

  • Hong, S. W. and Bergles, A. E., 1976 “Augmentation of Laminar Flow Heat Transfer in Tubes by Means of Twisted-Tape Inserts,”Journal of Heat Transfer, Vol. 98, pp. 251–256.

    Google Scholar 

  • Kaushik, N. and Azer, N. Z., 1986, “Heat Transfer Enhancement by Doubly Augmented Tubes,”Proceedings of the 8th International Heat transfer Conference, Vol. 6, pp. 2855–2860.

    Google Scholar 

  • Lee, S. C., Chung, M. and Shin, H. S., 1993, “Condensation Heat Transfer and Pressure Drop Performance of Horizontal Smooth and Internally-Finned tubes with Refrigerant 113,”Experimental Heat Transfer, Fluid Mechanics and Thermodynamics, Vol. 2, pp. 1349–1356.

    Google Scholar 

  • Li, H. M., Ye, K. S., Tan, Y. K. and Deng, S. J., 1982, “Investigation on the Tube Side Flow Visualization, Friction Factors and Heat Transfer Characteristics of Helical-Ridging Tubes,”Proceedings of the 7th International Heat Transfer Conference, Vol. 3, pp. 75–80.

    Google Scholar 

  • Lundberg, R. E., MeCuen, P. A. and Reynolds, W. C., 1963,Int. J. Heat Mass Transfer. Vol. 6, p. 495.

    Article  Google Scholar 

  • Obot, N. T., Esen, E. B., Snell, K. H. and Rabas, T. J., 1991, “Pressure Drop and Heat Transfer for Spirally Fluted Tubes Including Validation of the Role of Transition,”fouling and Enhancement Interactions, HTD-Vol. 164, pp. 85–92.

    Google Scholar 

  • Rabas, T. J. and Arman, B., 1992, “The Influence of the Prandtl number on the Thermal Performance of Tubes with the Separation and Reattachment Enhancement Mechanism,”Enhanced Heat Transfer, HTD-Vol. 202, pp. 77–87.

    Google Scholar 

  • Ravigururajan, T. S. and Bergles, A. E., 1986, “An Experimental Verification of General Correlations for Single Phase Turbulent Flow in Ribbed Tubes,”Advances in Heat Exchanger Design, HTD-Vol. 66, pp. 1–11.

    Google Scholar 

  • Ravigururajan, T. S. and Bergles, A. E., 1995, “Prandtl Number Influence on Heat Transfer Enhancement in Tubulent Flow of Water at Low Temperatures,”J. Heat Transfer, Vol. 117, pp. 276–282.

    Article  Google Scholar 

  • Richards, D. E., Grant, M. M. and Christensen, R. N., 1987, “Turbulent Flow and Heat Transfer Inside Doubly-Fluted Tubes,”ASHRAE Transaction, Vol. 93, Part 2, pp. 2011–2026.

    Google Scholar 

  • Uttawar, S. B. and Raja Rao, M., 1985. “Augmentation of Laminar Flow Heat Transfer in Tubes by Means of Wire Coil Inserts,”J. Heat Transfer, Vol. 105, pp. 930–935.

    Article  Google Scholar 

  • Webb, R. L., 1994,Principles of Enhanced Heat Transfer, John Wiley & Sons, New York.

    Google Scholar 

  • Webb, R. L., Eckert, E. R. G. and Goldstein, R. L., 1971, “Heat Transfer and Friction in Tubes with Repeated-Rib Roughness,”Int. J. Heat Mass Transfer, Vol. 14, pp. 601–617.

    Article  Google Scholar 

  • White, M. F. 1987,Fluid Mechanics, Mcgraw-Hill, New York, pp. 287–371.

    Google Scholar 

  • Withers, J. G., 1980, “Tube-Side Heat Transfer and Pressure Drop for Tubes having Helical Internal Ridging with Turbulent/Transition Flow of Single-Phase Fluid. Part 1. Single-Helix Riding,”Heat Transfer Engineering, Vol. 2, No. 1, pp. 48–58.

    Article  Google Scholar 

  • Yorkshire Imperial Metals, 1982, “YIM Heat Exchanger Tubes: Design Data for Horizontal Rope Tubes in Steam Condensers,” Technical Memorandum 3, Yorkshire Imperial Metals, Ltd., Leeds, United Kingdom.

    Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Rights and permissions

Reprints and permissions

About this article

Cite this article

Lee, S.C., Nam, S.C. & Ban, T.G. Performance of heat transfer and pressure drop in a spirally indented tube. KSME International Journal 12, 917–925 (1998). https://doi.org/10.1007/BF02945559

Download citation

  • Received:

  • Issue Date:

  • DOI: https://doi.org/10.1007/BF02945559

Key Words

Navigation