Heat transfer by forced convection from a cylinder to water in crossflow

Abstract This paper presents the results of an experimental investigation of heat transfer by forced convection from a cylinder to water in crossflow in the range of Reynolds numbers from approximately 104 to 105. The diameter of the test cylinder was 0.4375 in, and the temperature difference varied from 4 to 10 degF. The experimental data are in close agreement (mean deviation = 1 per cent) with the McAdams correlation, namely, (Nu) f =[0.35+0.56(Re) f 0.52 ](Pr) f 0.30 . McAdams derived his correlation equation from experimental data taken in the limited range of crossflow Reynolds numbers from 10−1 to 2 × 102. Purves and Brodkey infer from the Colburn analogy that McAdams' correlation is valid in the range of Reynolds number from 102 to 104. Therefore, on the basis of the present experimental data, it is concluded that McAdams' equation is valid in the extended range of Reynolds numbers from 10−1to 105. The present experimental data are equally well represented by (Nu) f =[0.35+0.34(Re) f 0.50 +0.15(Re) f 0.58 ](Pr) f 0.30 . In the latter equation, the term in (Re)f0.50 represents the heat transfer through the laminar boundary layer on the front portion of the cylinder, and the term in (Re)f0.58 accounts for the contribution to the total heat transfer from the back portion of the cylinder, where separation occurs. Either of the two equations given here may be used for design calculations, but the second equation is preferable in the the sense that it is more logically related to the physical processes involved.

[1]  J. Ulsamer,et al.  Die Wärmeabgabe eines Drahtes oder Rohres an einen senkrecht zur Achse strömenden Gas- oder Flüssigkeitsstrom , 1932 .

[2]  H. C. Perkins,et al.  Forced Convection Heat Transfer From a Uniformly Heated Cylinder , 1962 .

[3]  B. G. Van Der Hegge Zijnen,et al.  Heat transfer from horizontal cylinders to a turbulent air flow , 1958 .

[4]  H. Kramers,et al.  Heat transfer from spheres to flowing media , 1946 .

[5]  G. Leppert,et al.  Local heat-transfer coefficients on a uniformly heated cylinder , 1964 .

[6]  B. G. Van Der Hegge Zijnen,et al.  Modified correlation formulae for the heat transfers by natural and by forced convection from horizontal cylinders , 1956 .

[7]  A. H. Davis CIV. Convective cooling of wires in streams of viscous liquids , 1924 .

[8]  W. H. Giedt Effect of Turbulence Level of Incident Air Stream on Local Heat Transfer and Skin Friction on a Cylinder , 1951 .

[9]  E. W. Comings,et al.  Air Turbulence and transfer processes , 1948 .

[10]  G. Vliet,et al.  Forced Convection Heat Transfer From an Isothermal Sphere to Water , 1961 .

[11]  Edgar L. Piret,et al.  Heat Transmission from Fine Wires to Water - Low Velocity Data and Correlation , 1947 .

[12]  E. Schmidt,et al.  Wärmeabgabe über den Umfang eines angeblasenen geheizten Zylinders , 1941 .

[13]  P. Richardson ESTIMATION OF THE HEAT TRANSFER FROM THE REAR OF AN IMMERSED BODY TO THE REGION OF SEPARATED FLOW , 1962 .

[14]  R. A. Seban The Influence of Free Stream Turbulence on the Local Heat Transfer From Cylinders , 1960 .

[15]  Joseph Kestin,et al.  The influence of turbulence on the transfer of heat to cylinders near the stagnation point , 1961 .

[16]  J. Kestin,et al.  Influence of turbulence on transfer of heat from cylinders , 1957 .