Abstract
This study presents a series solution for computation of the steady state temperature field in circular ducts with prescribed wall heat flux. The ducts are filled with fluid saturated porous materials. The developed methodology includes a simple transformation that improves the convergence of this series solution. The acquired solution includes the contribution of axial conduction that leads to a modified Graetz-type solution for these fluid passages. Finally, this solution is augmented by the contribution of frictional heating.
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Abbreviations
- A m , B m :
-
Coefficient in a series
- Br :
-
Brinkman number \( \mu_{e} U^{2} /(r_{0} q_{w} ) \)
- c n :
-
Constants in Eq. 10
- c p :
-
Fluid specific heat (J/kg K)
- Da :
-
The Darcy number K/r 20
- D h :
-
Hydraulic diameter 2r 0 (m)
- F :
-
Transformation function, Eq. 6c
- h :
-
Heat transfer coefficient (W/m2 K)
- k :
-
Effective thermal conductivity (W/m K)
- I i , K i :
-
Modified Bessel functions with i = 0, 1 or 2
- K :
-
Permeability (m2)
- m, n:
-
Indices
- Nu D :
-
hD h /k
- Pe :
-
Peclet number Ur 0/α
- Pr :
-
Prandtl number μc p /k
- q w :
-
Wall heat flux when x ≥ 0 (W/m2)
- r :
-
\( \hat{r}/r_{0} \)
- r 0 :
-
Circular duct’s radius
- \( \hat{r} \) :
-
Radial coordinate (m)
- R :
-
Eigenfunction
- St :
-
Stanton number h/(ρc p U), Eq. 15c
- T i :
-
Fluid temperature as x → −∞ (K)
- T w :
-
Wall temperature (K)
- u :
-
Velocity (m/s)
- U :
-
Average velocity (m/s)
- x :
-
\( \hat{x}/r_{\,0} \)
- \( \hat{x} \) :
-
Axial coordinate (m)
- \( \bar{x} \) :
-
\( (\hat{x}/r_{{{\kern 1pt} 0}} )/Pe \)
- α :
-
Thermal diffusivity (m2/s)
- β m :
-
Eigenvalues
- θ :
- θ *:
-
k(T − T i )/q w r0
- λ m :
-
Eigenvalues
- μ :
-
Fluid viscosity (N s/m2)
- μ e :
-
Effective viscosity (N s/m2)
- ρ :
-
Fluid density (kg/m3)
- Φ m :
-
Eigenfunction R m (r) when x < 0
- Ψ m :
-
Eigenfunction R m (r) when x ≥ 0
- σ :
-
Parameter Pe/2
- ω :
-
\( {1 \mathord{\left/ {\vphantom {1 {\sqrt {MDa} }}} \right. \kern-\nulldelimiterspace} {\sqrt {MDa} }} \)
- 1, 2:
-
x < 0 or x ≥ 0
- b :
-
Bulk temperature
- s :
-
Source
- w :
-
Condition at the wall
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Appendix: Application of orthogonality condition
Appendix: Application of orthogonality condition
The objective of this analysis is to use the orthogonality condition for determination of A m in Eq. 8 and B m for insertion in Eq. 9. Replacing the parameter −λ 2 m with β 2 m and R m (r) with Φ m (r) in Eq. 8, it becomes
Also, replacing the parameter R m (r) with Ψ m (r) in Eq. 9, it becomes
Then, the compatibility conditions as given by Eqs. 13a, 13b leads to the relations
and
Next, one can multiply both sides of Eq. 28 by β 2 n /Pe 2 − u/U, both sides of Eq. 29 by 1/Pe 2, and add the resulting relations to get
To apply the orthogonality condition, one can multiply both sides of Eq. 30 by Φ n (r)rdr for any given n and integrate over r to produce
It is to be noted from the orthogonality condition in [8] that the first term on the right side of Eq. 31 would vanish since \( - \beta_{n}^{2} \ne \lambda_{m}^{2} \) as they are in different domains for the same eigenfunctions. Therefore, the non-zero terms when \( \beta_{n}^{2} = \beta_{m}^{2} \) for m = n lead to the value of
The aforementioned procedure can be modified for determination of coefficient B m for insertion in Eq. 9. Multiplying both sides of Eq. 28 by \( - \lambda_{n}^{2} /Pe^{2} - u/U \), both sides of Eq. 29 by 1/Pe 2, and then adding the resulting relations yields
Finally, multiplying both sides of Eq. 33 by Ψ n (r)rdr for a given n and integrating over r produces
In this case, the left side of Eq. 34 vanishes due to the orthogonality condition [8] since \( - \beta_{n}^{2} \ne \lambda_{m}^{2} \); therefore, the non-zero terms when \( \lambda_{n}^{2} = \lambda_{m}^{2} \) for m = n lead to the value of
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Haji-Sheikh, A., Minkowycz, W.J. & Manafzadeh, S. Axial conduction effect in flow through circular porous passages with prescribed wall heat flux. Heat Mass Transfer 46, 727–738 (2010). https://doi.org/10.1007/s00231-010-0617-3
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DOI: https://doi.org/10.1007/s00231-010-0617-3