Abstract
A flow and heat transfer numerical simulation is performed for a 2D laminar incompressible gas flow through a constricted microchannel in the slip regime with constant wall temperature. The effects of rarefaction, creeping flow, first order slip boundary conditions and hydrodynamically/thermally developing flow are assumed. The effects of Knudsen number and geometry on thermal and hydrodynamic characteristics of flow in a constricted microchannel are explored. SIMPLE algorithm in curvilinear coordinate is used to solve the governing equations including continuity, energy and momentum with the temperature jump and velocity slip conditions at the solid walls in discretized form. The resulting velocity and temperature profiles are then utilized to obtain the microchannel C f Re and Nusselt number as a function of Knudsen number and geometry. The results show that Knudsen number has declining effect on the C f Re and Nusselt number in the constricted microchannel. In addition, the temperature jump on wall and slip velocity increase with increasing Knudsen number. Moreover, by decreasing the throttle area, the fluid flow characteristics experience more intense variations in the constricted region. To verify the code a comparison is carried out with available results and good agreement is achieved.
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Abbreviations
- a :
-
Amplitude of the wave (m)
- k :
-
Thermal conductivity of air (W/m K)
- h :
-
Local heat transfer coefficient (W/m2 K)
- J :
-
Jacobian of the coordinate transformation
- p :
-
Dimensionless pressure
- Re :
-
Reynolds number (Re = ρu i L */μ)
- Pr :
-
Prandtl number (Pr = ν/α)
- Nu :
-
Local Nusselt number
- Nu ∞ :
-
Fully developed Nusselt number
- Kn :
-
Knudsen number
- Ma :
-
Mach number
- Pe :
-
Peclet number
- Ec :
-
Eckert number
- C f :
-
Skin-friction coefficient
- c p :
-
Specific heat (J/kg K)
- n :
-
Dimensionless normal direction to the wall
- s :
-
Dimensionless tangential direction to the wall
- q11, q22, q12:
-
Grid parameters
- R :
-
Gas constant (J/kg K)
- T :
-
Temperature (K)
- q″:
-
Heat flux
- u :
-
Dimensionless velocity component in x-direction
- v :
-
Dimensionless velocity component in y-direction
- L*:
-
Channel inlet width
- x :
-
Dimensionless horizontal coordinate
- y :
-
Dimensionless vertical coordinate
- α :
-
Thermal diffusivity (m2/s)
- λ :
-
Surface wavelength (m)
- ρ :
-
Density of fluid (kg/m3)
- μ :
-
Dynamic viscosity (kg/m s)
- γ :
-
Ratio of specific heats (cp/cv)
- λ :
-
Molecular mean free path (m)
- ν :
-
Kinematic viscosity (m2/s)
- σ T :
-
Energy accommodation coefficient
- σ ν :
-
Momentum accommodation coefficient
- θ :
-
Dimensionless temperature
- ξ :
-
Curvilinear horizontal coordinate
- η :
-
Curvilinear vertical coordinate
- τ :
-
Shear stress
- ave:
-
Mean value
- w :
-
Surface conditions
- i :
-
Inlet conditions
- s :
-
Fluid property near the wall
- C :
-
Contravariant velocities
- tang:
-
Tangential direction
- *:
-
Returns to dimensional parameters
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Shokouhmand, H., Bigham, S. & Nasr Isfahani, R. Effects of Knudsen number and geometry on gaseous flow and heat transfer in a constricted microchannel. Heat Mass Transfer 47, 119–130 (2011). https://doi.org/10.1007/s00231-010-0674-7
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DOI: https://doi.org/10.1007/s00231-010-0674-7