Abstract
The heat transfer characteristics of the thermally developing flow in the circular and parallel plates microchannels under the constant wall temperature and the constant heat flux are studied analytically. The energy equations are solved by using the separation of variables combined with the Gram–Schmidt orthogonalization. The effect of the number of eigenvalues on the calculation accuracy of the local Nusselt number is first determined. The temperature distribution and the heat transfer coefficient at the entrance region are calculated considering the effects of the rarefaction (0 < Kn < 0.1) and the axial heat conduction (Pe > 50). It is found that the axial heat conduction can dramatically improve the heat transfer of the thermally developing flow when the Peclet number is less than 250. But when the Peclet number is greater than 500, the effect of the axial heat conduction can be omitted. Enhancing the rarefaction would weaken the influence of the axial heat conduction on the heat transfer, and the difference of the local Nusselt number between the two boundary conditions decreases as increasing Kn. Enhancing fluid axial heat conduction would increase the thermal entrance length. The thermal entrance length of the microtube is 3–4 times that of the parallel plates microchannel, and the correlations of the thermal entrance lengths are developed, which may provide guidance for thermal design and optimization of microchannel heat sinks.
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Abbreviations
- c p :
-
Specific heat (J kg−1 K−1)
- C n :
-
Coefficient in Eq. (16)
- D h :
-
Hydraulic diameter (m)
- h :
-
Convective heat transfer coefficient (W m−2 K−1)
- k :
-
Parameter defined by Eq. (39)
- Kn :
-
Knudsen number
- Kn u :
-
Modified Knudsen number = Kn(2–σv)/σv
- Nu :
-
Nusselt number
- p :
-
Geometry parameter
- Pe :
-
Peclet number
- Pr :
-
Prandtl number
- Q :
-
Internal heat generation (W m−3)
- q :
-
Heat flux (W m−2)
- r :
-
R-Coordinate (m)
- T :
-
Temperature (K)
- u :
-
Fluid velocity (m s−1)
- x :
-
X-Coordinate (m)
- x*:
-
Non-dimensional length = x/(DhPe)
- y :
-
Y-Coordinate (m)
- β :
-
Coefficient of thermal expansion (K−1)
- γ :
-
Ratio of specific heats
- θ :
-
Dimensionless temperature
- κ :
-
Fluid thermal conductivity (W m−1 K−1)
- λ :
-
Mean free path (m)
- \({\uplambda }_{{\text{n}}}^{{2}}\) :
-
Eigenvalue
- μ :
-
Dynamic viscosity (N s m−2)
- ρ :
-
Fluid density (kg m−3)
- σ v :
-
Tangential momentum accommodation coefficient
- σ T :
-
Thermal accommodation coefficient
- Φ:
-
Viscous dissipation function
- \(\phi_{n}\) :
-
Eigenfunction
- ∞ :
-
Fully developed region
- c:
-
Microtube
- m:
-
Mean
- p:
-
Parallel plates microchannel
- w:
-
Wall
- in:
-
Inlet
- CM:
-
Circular microchannel
- PPM:
-
Parallel plates microchannel
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Acknowledgements
This research was supported by the Talents Special Fund of China Three Gorges University (No. 8210403).
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Appendix A: Steps of Gram-Schmidt orthogonalization to obtain C n
Appendix A: Steps of Gram-Schmidt orthogonalization to obtain C n
For the eigenfunctions sequence {ϕn}, assuming that the orthogonalized function sequences are {gn}, the relationship between the above two is as follows
For the orthogonal function sequences {gn}, there is the following orthogonal property when i ≠ j
Substituting (A-1) and (A-2) into (A-5) yields
then
More generally,
Based on the inlet boundary condition, setting the coefficient of the eigenfunctions after the orthogonalization is Bn, namely
and
The coefficient Bn can be obtained based on the characteristics of the orthogonal function:
According to (A-1)–(A-4), we have
After determining Bn, Cn can be calculated according to (A-9), that is
where
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Su, L., He, B. & Yu, W. Analytical solution of thermally developing heat transfer in circular and parallel plates microchannels. Sādhanā 47, 219 (2022). https://doi.org/10.1007/s12046-022-01951-x
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DOI: https://doi.org/10.1007/s12046-022-01951-x