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Unstable mixed convection in a heated inclined porous channel

Published online by Cambridge University Press:  06 August 2015

L. A. Sphaier*
Affiliation:
Department of Mechanical Engineering, Universidade Federal Fluminense – PGMEC/UFF, Rua Passo da Pátria 156, bloco E, sala 216, Niterói, RJ, 24210-240, Brazil
A. Barletta
Affiliation:
Department of Industrial Engineering, Alma Mater Studiorum Università di Bologna, Viale Risorgimento 2, 40136, Bologna, Italy
M. Celli
Affiliation:
Department of Industrial Engineering, Alma Mater Studiorum Università di Bologna, Viale Risorgimento 2, 40136, Bologna, Italy
*
†Email address for correspondence: lasphaier@id.uff.br

Abstract

This paper presents a stability analysis of a mixed convection problem in an inclined parallel-plate channel with uniform heating (or cooling) from the top and bottom. The channel is filled with a saturated homogeneous porous medium and the momentum equation is given by Darcy’s model. A forced through-flow is prescribed across the channel. Linear stability analysis is thus employed to determine the onset of thermoconvective instability. The channel inclination is shown to play an important role in the stability of the problem, where two different regimes can be present: a buoyancy-assisted regime and a buoyancy-opposed regime. The analysis of the problem leads to a differential eigenvalue problem composed of a system of four complex-valued equations that are used to determine the critical values of the Rayleigh number leading to an instability under different problem configurations. This eigenproblem is solved by employing the generalised integral transform technique (GITT), in which simpler real eigenfunction bases are used to expand the complex eigenproblem. The results indicate that the longitudinal rolls are always more unstable than oblique and transverse rolls. For a buoyancy-opposed regime, even with a very small channel inclination angle, the basic through-flow is always unstable. This result has an important implication for experimental research, as it shows that a perfect alignment must be employed for horizontal mixed-convection experiments to avoid instabilities that arise in the buoyancy-opposed regime.

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Type
Papers
Copyright
© 2015 Cambridge University Press 
Figure 0

Figure 1. Sketch of the system.

Figure 1

Table 1. Critical Rayleigh number, wavenumber and modified angular frequency for different truncation orders, for $\mathit{Pe}\rightarrow \infty$, and different values of ${\it\phi}$ and ${\it\gamma}$.

Figure 2

Table 2. Critical Rayleigh number, wavenumber and modified angular frequency for different truncation orders, for $\mathit{Pe}=50$, and different values of ${\it\phi}$ and ${\it\gamma}$.

Figure 3

Figure 2. Buoyancy-assisted flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with different Péclet numbers and inclination angles for longitudinal rolls (${\it\gamma}=0$): (a) $Pe=\infty$, (b) 500, (c) 100, (d) 50, (e) 25, (f) 20.

Figure 4

Figure 3. Buoyancy-opposed flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with different Péclet numbers and inclination angles for longitudinal rolls (${\it\gamma}=0$): (a) $Pe=-500$, (b) $-100$, (c) $-50$, (d) $-25$, (e) $-10$, (f) $-1$.

Figure 5

Figure 4. Buoyancy-assisted flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with different Péclet numbers and values of ${\it\gamma}$ for ${\it\phi}=5^{\circ }$: (a) $Pe=500$, (b) 100, (c) 50, (d) 25.

Figure 6

Figure 5. Buoyancy-assisted flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with different Péclet numbers and values of ${\it\gamma}$ for ${\it\phi}=15^{\circ }$: (a) $Pe=500$, (b) 100, (c) 50, (d) 25.

Figure 7

Figure 6. Buoyancy-assisted flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with different Péclet numbers and values of ${\it\gamma}$ for ${\it\phi}=30^{\circ }$: (a) $Pe=500$, (b) 100, (c) 50, (d) 25.

Figure 8

Figure 7. Buoyancy-opposed flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with $\mathit{Pe}=500$ and ${\it\phi}=30^{\circ }$ and different values of ${\it\gamma}$.

Figure 9

Figure 8. Buoyancy-opposed flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with different Péclet numbers and values of ${\it\gamma}$ for ${\it\phi}=5^{\circ }$: (a) $Pe=-500$, (b) $-100$, (c) $-50$, (d) $-25$.

Figure 10

Figure 9. Buoyancy-opposed flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with different Péclet numbers and values of ${\it\gamma}$ for ${\it\phi}=15^{\circ }$: (a) $Pe=-500$, (b) $-100$, (c) $-50$, (d) $-25$.

Figure 11

Figure 10. Buoyancy-assisted flow: neutral stability curves in the plane $(a,\mathit{Ra}\cos {\it\phi})$ with different Péclet numbers and values of ${\it\gamma}$ for ${\it\phi}=30^{\circ }$: (a) $Pe=-500$, (b) $-100$, (c) $-50$, (d) $-25$.

Figure 12

Figure 11. Critical Rayleigh number, $\mathit{Ra}_{c}$, versus $\mathit{Pe}$ with different inclination angles for: (a) longitudinal (${\it\gamma}=0$), (b) oblique (${\it\gamma}=1/3$), (c) oblique ($2/3$) and (d) transverse (${\it\gamma}=1$) rolls in buoyancy-assisted flow.