Air-Side Heat Transfer and Friction Correlations for Plain Fin-and-Tube Heat Exchangers With Staggered Tube Arrangements

Author:

Kim N. H.1,Youn B.2,Webb R. L.3

Affiliation:

1. Department of Mechanical Engineering, University of Inchon, 177 Dohwa-Dong, Nam-Gu, Inchon 402-749, Korea

2. Air Conditioning & Refrigeration Division, Samsung Electronics, Korea

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

Abstract

This paper deals with heat exchangers having plain fins on a staggered array of circular tubes. Correlations are developed to predict the air-side heat transfer coefficient and friction factor as a function of the Reynolds number and geometric variables of the heat exchanger such as tube diameter, tube pitch, fin spacing, etc. A multiple regression technique was used to correlate 47 sets of heat exchanger data to develop the heat transfer and friction correlation. The correlations are applicable to heat exchangers having small diameter tubes (or large tube pitch to tube diameter ratio), whose performance previous correlations failed to predict adequately. The heat transfer correlation applicable to three or more row configuration predicts 94 percent of the data within ±20 percent, and the heat transfer correlation applicable to one- or two-row configuration predicts 94 percent of the data within ±20 percent. The friction correlation predicts 90 percent of the data within ±20 percent.

Publisher

ASME International

Subject

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

Reference34 articles.

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2. Cox, B., and Jallouk, P. A., 1982, “Experimental Data on the Performance Characteristics of Eight Compact Heat Transfer Surfaces,” Report K-1832, Union Carbide Corp., Oak Ridge, TN.

3. Dittus, F. W., and Boelter, L. M. K., 1930, Publications on Engineering, University of California, Berkeley, Vol. 2, p. 443.

4. Elmahdy A. H. , and BriggsR. C., 1979, “Finned Tube Heat Exchangers; Correlation of Dry Surface Data,” ASHRAE Trans., Vol. 85, No. 2, pp. 262–273.

5. Gnielinski, V., 1976, “New Equation for Heat and Mass Transfer in Turbulent Pipe and Channel Flow,” Int. Chem. Engng., pp. 359–368.

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