Abstract
Analysis of combined free and forced convection through vertical noncircular ducts is carried out using a variational technique. Fully developed flow with uniform axial heat input and uniform peripheral heat flux is assumed. All fluid properties are considered invariant with temperature except the variation of density in the buoyancy term of the equation of motion. The condition of uniform peripheral heat flux is utilized in deriving the variational expression. This procedure releases the thermal boundary condition from satisfying exactly the condition at the wall. A finite-difference procedure is carried out. For pure forced convection case, a particularly simple variational expression is presented. Nusselt numbers for combined free and forced convection are computed for rectangular, rhombic and elliptical ducts. An exact solution is presented for laminar forced convection through elliptic ducts. Variational results are in agreement with this exact solution. The present results are compared with those in the published literature wherever possible, and good agreement is obtained.
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Abbreviations
- A :
-
area of cross-section
- a, b :
-
semi axes
- C p :
-
specific heat of the fluid at constant pressure
- C 1 :
-
temperature gradient in flow direction,∂T/∂Z
- C 2 :
-
heat flux normal to surface,∂φ/∂N
- D h :
-
hydraulic diameter, (4× cross-sectional area)/(heat transfer perimeter)
- F :
-
heat generation parameter, dimensionless,Q/ρC p C 1 U
- g :
-
gravitational, acceleration
- L :
-
pressure drop parameter, dimensionless
- Nu :
-
hD h/κ, Nusselt number, dimensionless
- P :
-
heat transfer perimeter
- Q :
-
heat generation rate
- Ra :
-
Rayleigh number, dimensionless, (ρ 2 gC p C 1 βD 4 h )/κμ
- S :
-
duct circumference
- T :
-
temperature
- u :
-
axial velocity
- U :
-
average axial velocity
- V :
-
dimensionless axial velocity,u/U
- x, y, X, Y :
-
rectangular co-ordinates,X=x/D h,Y=y/D h
- z :
-
axial co-ordinate in flow direction
- φ :
-
dimensionless temperature function,\({{(T - T_{ref} )} \mathord{\left/ {\vphantom {{(T - T_{ref} )} {\left[ {\frac{{\rho UC_p C_1 D_h^2 }}{\kappa }} \right]}}} \right. \kern-\nulldelimiterspace} {\left[ {\frac{{\rho UC_p C_1 D_h^2 }}{\kappa }} \right]}}\)
- β, ρ, κ, μ :
-
the fluid properties in standard notation
- ψ :
-
aspect ratio,b/a
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Iqbal, M., Khatry, A.K. & Aggarwala, B.D. On the second fundamental problem of combined free and forced convection through vertical noncircular ducts. Appl. Sci. Res. 26, 183–208 (1972). https://doi.org/10.1007/BF01897849
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DOI: https://doi.org/10.1007/BF01897849