Abstract
A finite-volume numerical model is constructed and applied to evaluate the time-dependent heat-transfer characteristics of longitudinal fins with a rectangular profile. To facilitate comparisons with analytical solutions, the problem is taken to be one-dimensional with constant thermal properties. Two base boundary conditions are considered: (1) a step change and (2) a periodic change in temperature. Parametric studies are carried out to investigate the effects of grid size, time step, fin parameter, Fourier number, amplitude and frequency of base-temperature oscillation on the fin temperature distribution, heat-transfer rate and efficiency. The study shows an excellent agreement between the numerical and analytical results and investigates the importance of the initial transient effects.
Zusammenfassung
Ein numerisches Finit-Volumen-Modell wird aufgestellt und zur Ermittlung des zeitabhängigen Wärmeübergangsverhaltens langer Rechteckrippen herangezogen. Um den Vergleich mit analytischen Lösungen zu erleichtern, soll das Problem eindimensional mit konstanten Stoffwerten vorausgesetzt sein. Als Randbedingungen werden aufgeprägt: (1) ein Temperatursprung und (2) eine periodische Temperaturänderung. Parameterstudien zeigen den Einfluß der Maschenweite, des Zeitschrittes, des Rippenparameters, der Fourierzahl, der Amplitude und Frequenz der Fußtemperaturschwingung auf die Verteilung der Rippentemperatur, des übergehenden Wärmestroms und den Wirkungsgrad. Die Studie ergab ausgezeichnete Übereinstimmung zwischen den numerischen und analytischen Ergebnissen. Ferner wird der Einfluß der anfänglichen transienten Effekte untersucht.
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Abbreviations
- A :
-
dimensionless amplitude of base temperature oscillation
- B :
-
dimensionless frequency,ω L 2/α
- c :
-
specific heat
- DT :
-
a finite increment of time
- Fo :
-
Fourier number,αt/L 2
- h :
-
heat-transfer coefficient
- k :
-
thermal conductivity
- L :
-
fin length
- N :
-
dimensionless fin parameter, (2hL 2/kδ)1/2
- NJ :
-
number of finite-difference grid nodes along the fin
- q*:
-
normalized rate of fin base heat flow,q b /q norm
- q :
-
heat-transfer rate
- q norm :
-
normalizing factor,kδ(T m −T ∞)/L
- t :
-
time
- T :
-
temperature
- y :
-
axial distance along the fin
- Y :
-
dimensionless distance,y/L
- α :
-
thermal diffusivity,k/ϱc
- δ :
-
fin thickness
- δt, Δt :
-
a finite increment of time
- δy :
-
relates to axial dimension of a node, Fig. 1
- η :
-
instantaneous fin efficiency,q b /2hL(T b −T ∞)
- ϑ :
-
=(T−T ∞)/(T b −T ∞), for a sudden change inT b =(T−T ∞)/(T m −T ∞), for a periodic change inT b
- ϱ :
-
density
- ω :
-
frequency of base temperature oscillation
- b :
-
base
- i :
-
initial
- m :
-
mean
- ∞:
-
ambient
- old:
-
relates to previous time step
- -:
-
average
References
Yang, J. W.: Periodic heat transfer in straight fins. J. Heat Transfer 94 (1972) 310–314
Suryanarayana, N. V.: Transient response of straight fins. J. Heat Transfer 97 (1975) 417–423
Mujahid, A.: Analysis of performance of a straight fin with oscillating base heat flux and environment temperature. J. Eng. Sci., King Saud University 13(1) (1987) 25–37
Aziz, A.; Na, T. Y.: Steady periodic heat transfer in fins of arbitrary profile. Num. Heat Transfer 3 (1980) 331–344
Mujahid, A.; Abu-Abdou, K.: Thermal performance of annular fins of arbitrary profile subjected to periodic base and environment temperatures. J. King Saud Univ. 5, Eng. Sci. (1) (1993) 105–122
Abu-Abdou, K.; Mujahid, A.: Heat transfer in straight fins of arbitrary profile subjected to periodic base and environment temperatures. Wärme-Stoffübertrag. 24 (1989) 353–361
Myers, G. E.: Analytical methods in conduction heat transfer. New York: McGraw-Hill 1971
Gosman, A. D.; Launder, B. E.; Reece, G. L.: Computer aided engineering heat transfer and fluid flow. Chichester: Ellis Horwood 1985
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Al-Sanea, S.A., Mujahid, A.A. A numerical study of the thermal performance of fins with time-dependent boundary conditions, including initial transient effects. Wärme - und Stoffübertragung 28, 417–424 (1993). https://doi.org/10.1007/BF01577883
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DOI: https://doi.org/10.1007/BF01577883