Abstract
A finite difference method is used to predict the performance of convecting-radiating fins of rectangular, trapezoidal, triangular, and concave parabolic shapes. The analysis assumes one-dimensional, steady conduction in the fin and neglects radiative exchange between adjacent fins and between the fin and its primary surface. For the range of thermal and geometrical parameters investigated, the variation of heat transfer rate and the fin efficiency with other profile shapes was found to be within 11 percent of the rectangular shape. The effect of profile shape is most pronounced when the Biot number,Bi, and radiation number,N r, are small compared to unity. Because of several limiting assumptions, the results would be used only for preliminary analysis and design particularly when a fin assembly is involved rather than an individual fin.
Zusammenfassung
Ein Finite-Differenzen-Verfahren findet Anwendung zur Berchnung der Wärmeübertragungsleistung mittels Konvektion und Strahlung an Rippen, die rechteckige, trapezförmige, dreieckige und konkav-parabolische Formen besitzen. Die Berechnungen setzen eine eindimensionale, stetige Wärmeleitung in den Rippen voraus und vernachlässigen den Strahlungsaustausch zwischen aneinandergrenzenden Rippen und zwischen den Rippen und ihrer Oberfläche. Für den betrachteten Bereich der thermischen und geometrischen Parameter wurde herausgefunden, daß die Veränderung der Wärmeübertragungsrate und des Rippenwirkungsgrades der anderen Profilformen im Bereich von 11 Prozent im Vergleich zur Rechteckform liegen. Der Einfluß der Profilform ist am stärksten, wenn die Biot-ZahlBi und die StrahlungszahlN r im Vergleich zu 1 klein sind. Aufgrund einiger einschränkender Annahmen sollten die Ergebnisse nur für die Voruntersuchungen und den Vorentwurf benutzt werden, insbesondere wenn es sich um eine Rippenanordnung und nicht um eine Einzelrippe handelt.
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Abbreviations
- A (x):
-
fin cross sectional are atx
- Bi :
-
Biot number based on one half base thickness =h w b/2k
- F :
-
vector representing the finite difference equation
- h :
-
convective heat transfer coefficient
- i :
-
subscript denoting the grid point
- J :
-
Jacobian
- k :
-
thermal conductivity of fin material
- L :
-
fin length
- n :
-
superscript denoting the iteration number
- N r :
-
radiation-conduction number =ε σ w b T 3 b /2k
- N R :
-
alternate radiation-conduction number =2L 2 ε σ T 3 b k w b =α 2 N r
- N CV :
-
alternate convection-conduction number = 2h L 2/k w b =α 2 Bi
- q :
-
heat transfer rate
- Q :
-
dimensionless heat transfer rateQ=q/kT b
- T :
-
temperature
- T b :
-
fin base temperature
- T s :
-
effective sink temperature for radiation
- T ∞ :
-
environment temperature for convection
- w b :
-
fin thickness at the base
- w t :
-
fin thickness at the tip
- w(x):
-
fin thickness at distancex
- W(ξ):
-
dimensionless thickness =w(x)/w b
- α :
-
ratio of length to one-half base thickness = 2L/w b
- β :
-
ratio of tip to base thickness =w t /w b
- ε :
-
surface emissivity
- Θ :
-
dimensionless temperature =T/T b
- Θ ∞ :
-
dimensionless convective environment temperature =T ∞/T b
- Θ s :
-
dimensionless sink temperature for radiation =T s /T b
- σ :
-
Stefan-Boltzmann constant
- η :
-
fin efficiency
- ξ :
-
dimensionless distance =x/L
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Nguyen, H., Aziz, A. Heat transfer from convecting-radiating fins of different profile shapes. Wärme- und Stoffübertragung 27, 67–72 (1992). https://doi.org/10.1007/BF01590120
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DOI: https://doi.org/10.1007/BF01590120