Abstract
The paper provides a numerical investigation of the entropy generation analysis due to mixed convection with viscous dissipation effect of a laminar viscous and incompressible fluid, flowing in an inclined channel filled with a saturated porous medium. The Darcy–Brinkman model is employed. The Navier–Stokes and energy equations are solved by classic Boussinesq incompressible approximation. A special attention is given to the study of the influence of the channel inclination angle on the transient and the steady-state entropy generation. The fluctuations of the transient total entropy generation are investigated when the inclination angle is varied from \(0^{\circ }\) to \(180^{\circ }\). Moreover, the entropy generation and the Bejan number were studied as a function of the inclination angle of the channel, in the steady state of mixed convection. It was found that the total entropy generation is maximum at inclination angle close to \(70^{\circ }\) and minimum at \(0^{\circ }\) and \(180^{\circ }\).
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Abbreviations
- c :
-
Specific heat capacity at constant pressure \((\hbox {m}^{2}{\cdot }\hbox {s}^{-2}{\cdot }\hbox {K}^{-1})\)
- Da :
-
Darcy number \((\mu /h^{2})\)
- g :
-
Gravitational acceleration \((\hbox {m}{\cdot }\hbox {s}^{-2})\)
- h :
-
Channel height (m)
- l :
-
Channel length (m)
- Nu :
-
The local Nusselt number \((\vert \hbox {d}\theta /\hbox {d}Y\vert )\)
- \({\overline{Nu}}\) :
-
The space-averaged Nusselt number
- \(\langle {\overline{Nu}}\rangle \) :
-
Space and time-averaged Nusselt number
- p :
-
Pressure \((\hbox {N}{\cdot }\hbox {m}^{-2})\)
- P :
-
Dimensionless pressure
- Pe :
-
Peclet number \(({\textit{Re}}{\cdot }{\textit{Pr}})\)
- Pr :
-
Prandtl number \((\eta c_{p}/\lambda _\mathrm{m})\)
- Ra :
-
Rayleigh number in porous media \((\beta g\Delta Th^{3}/(\upsilon {\cdot }\alpha _{\mathrm{eff}}))\)
- Re :
-
Reynolds number \(({hu}_{0}/\upsilon )\)
- \({\varvec{s}}\) :
-
Local entropy generation \((\hbox {J}{\cdot }\hbox {m}^{-3}{\cdot }\hbox {s}^{-1}{\cdot }\hbox {K}^{-1})\)
- \({\varvec{s}}_\mathrm{t}\) :
-
Total dimensionless entropy generation \((\hbox {J}{\cdot }\hbox {s}^{-1}{\cdot }\hbox {K}^{-1})\)
- \(\langle {\varvec{s}}_\mathrm{t}\rangle \) :
-
Time-averaged total entropy generation \((\hbox {J}{\cdot }\hbox {s}^{-1}{\cdot }\hbox {K}^{-1})\)
- t :
-
Time (s)
- T :
-
Temperature (K)
- \(T_{0}\) :
-
Mean temperature \([({T}_{\mathrm{h}}+ {T}_{\mathrm{c}})/2]\,(\hbox {K})\)
- \(\Delta T\) :
-
Temperature difference \(({T}_{\mathrm{h}}-{T}_{\mathrm{c}})\)
- \(u_{0}\) :
-
Characteristic velocity \((\hbox {m}{\cdot }\hbox {s}^{-1})\)
- u, v :
-
Velocity components in x and y directions, respectively \((\hbox {m}{\cdot }\hbox {s}^{-1})\)
- U, V :
-
Dimensionless velocity components
- x, y :
-
Cartesian coordinates (m)
- X, Y :
-
Dimensionless Cartesian coordinates
- \(\beta _\mathrm{T}\) :
-
Thermal volumetric expansion coefficient \((\hbox {K}^{-1})\)
- \(\varepsilon \) :
-
Medium porosity
- \(\mu \) :
-
Permeability of the porous media \((\hbox {m}^{2})\)
- \(\lambda \) :
-
Thermal conductivity \((\hbox {kg}{\cdot }\hbox {m}{\cdot }\hbox {s}^{-3}{\cdot }\hbox {K}^{-1})\)
- \(\theta \) :
-
Dimensionless temperature
- \(\varTheta \) :
-
Dimensionless period
- \(\uprho \) :
-
Mass density \((\hbox {kg}{\cdot }\hbox {m}^{-3})\)
- \(\uprho _{0}\) :
-
Reference mass density \((\hbox {kg}{\cdot }\hbox {m}^{-3})\)
- \(\upsigma \) :
-
Specific heat capacities ratio \(((\uprho \hbox {c})_{\mathrm{m}}/(\uprho \hbox {c})_{\mathrm{f}})\)
- \(\varLambda \) :
-
Viscosity ratio \((\eta _{\mathrm{eff}}/\eta )\)
- \(\eta \) :
-
Dynamic viscosity \((\hbox {kg}{\cdot }\hbox {m}^{-1}{\cdot }\hbox {s}^{-1})\)
- \(\upalpha \) :
-
Thermal diffusivity \((\hbox {m}^{2}{\cdot }\hbox {s}^{-1})\)
- \(\upsilon \) :
-
Kinematic viscosity \((\hbox {m}^{2}{\cdot }\hbox {s}^{-1})\)
- \(\uptau \) :
-
Dimensionless time
- a:
-
Dimensionless
- c:
-
Cold wall
- eff:
-
Effective
- F:
-
Fluid friction
- f:
-
Fluid
- H:
-
Heat transfer
- h:
-
Hot wall
- l:
-
Local
- m:
-
Porous media
- s:
-
Solid
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Tayari, A., Brahim, A.B. & Magherbi, M. Second Law Analysis in Mixed Convection Through an Inclined Porous Channel. Int J Thermophys 36, 2881–2896 (2015). https://doi.org/10.1007/s10765-015-1925-0
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DOI: https://doi.org/10.1007/s10765-015-1925-0