Abstract
Convection heat transfer (including natural and forced convection) of elliptical tubes had been studied system-atically. The experienced formula of heat transfer had been given. It presents fin efficiency of rectangular finned elliptical tube and optimized fin geometry (i.e. length/width ratio) and fin spacing for rectangular fin.
Zusammenfassung
Konvektion und Wärmeübergang (sowohl bei freier als auch bei erzwungener Konvektion) an elliptischen Rohren wurden systematisch untersucht. Es wird eine aus dem Experiment abgeleitete Beziehung für den Wärmeübergang angegeben, die den Gütegrad elliptischer Rohre mit Rechteckrippen unter optimierter Rippengeometrie (Längen- zu Breitenverhältnis und Rippenabstand) beinhaltet. Stichworte: Konvektiver Wärmeübergang, Rippengütegrad, Elliptische Rohre mit Rechteckrippe.
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Abbreviations
- A :
-
length of a rectangular fin
- A F :
-
\( = AB = \frac{\pi }{4}ab\) area of a fin
- A f :
-
overall fin area of per length
- A r :
-
tube surface of per length
- B :
-
width of a rectangular fin
- Gr :
-
\( = \frac{{\beta g\Delta T \cdot l^3 }}{{v^2 }}\) Grashof number
- N :
-
fin number of per length
- Nu :
-
=hl/λ Nusselt number
- Pr :
-
Prandtl number
- Ra :
-
=Gr·Pr Rayleigh number
- Re :
-
=wl/ν Reynolds number
- S 1 :
-
transverse tube pitch
- S 2 :
-
longitudinal tube pitch
- w :
-
fluid velocity
- a :
-
long axis of a ellipse
- b :
-
short axis of a ellipse
- c :
-
=a/b shape factor
- d e :
-
equivalent diameter
- g :
-
acceleration of gravity
- h :
-
heat exchange coefficient
- l :
-
characteristic length
- t :
-
fin spacing
- β:
-
coefficient of thermal expansion
- δ:
-
fin thickness
- η fm :
-
area average fin efficiency
- λ:
-
coefficient of fluid thermal conductivity
- λ f :
-
fin's thermal conductivity
- ν:
-
kinematic viscosity
References
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Chuchill, S. M.;Usagai, R. A. General Expression for the Correlation of Rates of Transfer and Other Phenomena. A.l.Ch.E. Journal 18(6) (1992) 1121–1128
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Suyi, H., Shizhou, P. Convection and heat transfer of elliptical tubes. Heat and Mass Transfer 30, 411–415 (1995). https://doi.org/10.1007/BF01647445
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DOI: https://doi.org/10.1007/BF01647445