Estimation of heat transfer coefficient on the fin of annular-finned tube heat exchangers in natural convection for various fin spacings

Abstract The finite difference method in conjunction with the least-squares scheme and experimental temperature data is used to predict the average heat transfer coefficient and fin efficiency on the fin of annular-finned tube heat exchangers in natural convection for various fin spacings. The radiation and convection heat transfer coefficients are simultaneously taken into consideration in the present study. The heat transfer coefficient on this annular circular fin is assumed to be non-uniform. Thus the whole annular circular fin is divided into several sub-fin regions in order to predict the average heat transfer coefficient h ¯ and fin efficiency from the knowledge of the ambient temperature, tube temperature and fin temperature recordings at several selected measurement locations. The results show that the h ¯ value increases with increasing the fin spacing S, and the fin efficiency decreases with increasing the fin spacing S. However, these two values respectively approach their corresponding asymptotical values obtained from a single fin as S → ∞. The fin temperature departs from the ideal isothermal situation and decreases more rapidly away from the circular center with increasing the fin spacing. In order to validate the accuracy of the present inverse scheme, a comparison of the average heat transfer coefficient on the fin between the present estimates and those obtained from the correlation recommended by current textbooks is made.

[1]  Han-Taw Chen,et al.  Investigation of natural-convection heat transfer coefficient on a vertical square fin of finned-tube heat exchangers. , 2006 .

[2]  F. Saboya,et al.  Performance of one- and two-row tube and plate fin heat exchangers , 1984 .

[3]  Jiin-Yuh Jang,et al.  Local heat transfer measurements of plate finned-tube heat exchangers by infrared thermography , 2002 .

[4]  A. Nowak,et al.  Inverse thermal problems , 1995 .

[5]  W. Rohsenow,et al.  Handbook of Heat Transfer Fundamentals , 1985 .

[6]  V. Morgan The Overall Convective Heat Transfer from Smooth Circular Cylinders , 1975 .

[7]  J. P. Hartnett,et al.  Handbook of Heat Transfer Fundamentals (Second Edition) , 1986 .

[8]  Yue-Tzu Yang,et al.  The inverse estimation of the thermal boundary behavior of a heated cylinder normal to a laminar air stream , 2000 .

[9]  Charles Dingee Jones,et al.  Optimum Arrangement of Rectangular Fins on Horizontal Surfaces for Free-Convection Heat Transfer , 1970 .

[10]  J. L. Lage TUBE-TO-TUBE HEAT TRANSFER DEGRADATION EFFECT ON FINNED-TUBE HEAT EXCHANGERS , 2001 .

[11]  Stuart W. Churchill,et al.  Correlating equations for laminar and turbulent free convection from a horizontal cylinder , 1975 .

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

[13]  S. Yildiz,et al.  An experimental investigation on performance of annular fins on a horizontal cylinder in free convection heat transfer , 2004 .

[14]  Y. Jaluria,et al.  An Introduction to Heat Transfer , 1950 .

[15]  Han-Taw Chen,et al.  Prediction of heat transfer coefficient on the fin inside one-tube plate finned-tube heat exchangers , 2005 .

[16]  F. Kreith,et al.  Principles of heat transfer , 1962 .

[17]  Dong-Hoon Choi,et al.  OPTIMUM DESIGN OF PLATE HEAT EXCHANGER WITH STAGGERED PIN ARRAYS , 2004 .