Heat Transfer and Friction Characteristics of Internal Helical-Rib Roughness

Author:

Webb R. L.1,Narayanamurthy R.2,Thors P.2

Affiliation:

1. Department of Mechanical Engineering, Pennsylvania State University, University Park, PA 16802

2. Wolverine Tube, Decatur, AL 35609

Abstract

This paper provides heat transfer and friction data for single-phase flow in seven 15.54-mm inside diameter tubes having internal helical-rib roughness. The range of geometric parameters were number of rib starts (18 to 45), helix angle (25 to 45 deg), and rib height (0.33 to 0.55 mm). These geometries provide data on a new class of internal enhancement that is typical of commercially rough tubes presently used. The tested geometries provide enhancement by flow separation at the ribs, and by a significant surface area increase. The data were taken with water having 5.08⩽Pr⩽6.29. Two different correlations were employed to predict the Stanton number and friction factor as a function of geometric variables and Reynolds number. The average deviation of the multiple regression heat transfer and correlations were 2.9 percent and 3.8 percent, respectively. Heat transfer and friction correlations based on the heat-momentum transfer analogy for rough surfaces yielded standard deviations of 1.4 percent and 5.4 percent, respectively. The correlations were shown to reasonably predict the heat transfer and friction for commercially used helical-rib roughened tubes. [S0022-1481(00)03001-2]

Publisher

ASME International

Subject

Mechanical Engineering,Mechanics of Materials,Condensed Matter Physics,General Materials Science

Reference9 articles.

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

3. Gee, D. L., and Webb, R. L., 1980, “Forced Convection Heat Transfer in Helically Rib-Roughened Tubes,” Int. J. Heat Mass Transf., 23, pp. 1127–1136.

4. Briggs, D. E., and Young, E. H., 1969, “Modified Wilson Plot Techniques for Obtaining Heat Transfer Correlations for Shell and Tube Heat Exchangers,” Chem. Eng. Prog. Symp. Ser., No. 92, 65, pp. 35–45.

5. Seider, E. N., and Tate, G. E., 1936, “Heat Transfer and Pressure Drop of Liquids in Tubes,” Ind. Eng. Chem., 28, p. 14291429.

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