Air-Side Heat Transfer in Finned Tube Heat Exchangers

Because of the low heat transfer coefficient of gases, it is necessary to use extended surfaces on the gas side when exchanging heat with liquids or two-phase fluids. Such finned tube exchangers are a very important basic class of heat exchangers. Although finned tube exchangers have been in existence for 50 yr, there have been numerous developments in the technology. This paper attempts to survey the recent developments related to the air-side aspects of heat exchanger design. Nearly all of the recent developments have been empirical because of the complicated gas-side flow structure. Among the developments discussed are the use of special surface geometries for enhanced heat transfer, row effects, local heat transfer coefficient distribution, and correlations for heat transfer coefficient and pressure drop. Two important design configurations—circular finned tubes and plate fin designs—are considered separately.

[1]  V. B. Kuntish,et al.  Effect of the relative depth of the interfin space on heat transfer from bundles of finned tubes , 1974 .

[2]  E. Sparrow,et al.  Experiments on the Transfer Characteristics of a Corrugated Fin and Tube Heat Exchanger Configuration , 1976 .

[3]  E. H. Young,et al.  Heat transfer and pressure drop of air in forced convection across triangular pitch banks of finned tubes , 1958 .

[4]  Herman H Ellerbrock,et al.  Surface heat-transfer coefficients of finned cylinders , 1939 .

[5]  A. London,et al.  Compact heat exchangers , 1960 .

[6]  D. R. Tree,et al.  Heat-Transfer and Flow-Friction Data for Two Fin—Tube Surfaces , 1971 .

[7]  E. Sparrow,et al.  Heat/mass transfer characteristics for flow in a corrugated wall channel. , 1977 .

[8]  Ephraim M Sparrow,et al.  Transfer characteristics of two-row plate fin and tube heat exchanger configurations , 1976 .

[9]  M. Smith,et al.  Airflow Phenomena in the Louvered-Fin Heat Exchanger , 1973 .

[10]  Ephraim M Sparrow,et al.  Mass-transfer experiments on secondary-flow vortices in a corrugated wall channel , 1976 .

[11]  F. K. Moore,et al.  Analysis of Large Dry Cooling Towers With Power-Law Heat Exchanger Performance , 1976 .

[12]  H. Schlichting Boundary Layer Theory , 1955 .

[13]  Franz J. Schulenberg,et al.  Finned Elliptical Tubes and Their Application in Air-Cooled Heat Exchangers , 1966 .

[14]  Ephraim M Sparrow,et al.  Experiments on a Three-Row Fin and Tube Heat Exchanger , 1976 .

[15]  H. Brauer Wärme‐ und strömungstechnische Untersuchungen an quer angeströmten Rippenrohrbündeln. Teil 1: Versuchsanlagen und Meßergebnisse bei höheren Drucken , 1961 .

[16]  C. Weierman,et al.  Correlations Ease the Selection of Finned Tubes , 1976 .

[17]  J. A. Hitchcock,et al.  A STUDY OF THE HEAT TRANSFER PROCESSES IN BANKS OF FINNED TUBES IN CROSS FLOW, USING A LARGE SCALE MODEL TECHNIQUE. , 1967 .

[18]  A. Lapin,et al.  Heat Transfer Coefficients for Finned Exchangers , 1959 .

[19]  Ephraim M Sparrow,et al.  Local and average transfer coefficients for one-row plate fin and tube heat exchanger configurations , 1974 .