Abstract
The problem of combined conduction-mixed convection-surface radiation from a vertical electronic board provided with three identical flush-mounted discrete heat sources is solved numerically. The cooling medium is air that is considered to be radiatively transparent. The governing equations for fluid flow and heat transfer are converted from primitive variable form to stream function-vorticity formulation. The equations, thus obtained, are normalised and then are converted into algebraic form using a finite volume based finite difference method. The resulting algebraic equations are then solved using Gauss–Seidel iterative method. An optimum grid system comprising 151 grids along the board and 111 grids across the board is chosen. The effects of various parameters, such as modified Richardson number, surface emissivity and thermal conductivity on temperature distribution along the board, maximum board temperature and relative contributions of mixed convection and radiation to heat dissipation are studied in detail. Further, the contributions of free and forced convection components of mixed convection to board temperature distribution and peak board temperature are brought out. The exclusive roles played by surface radiation and buoyancy in the present problem are clearly elucidated.
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Abbreviations
- A r1, A r2 :
-
geometric ratios, L/t and L/L h, respectively
- g :
-
acceleration due to gravity (9.81 m/s2)
- Gr *L :
-
modified Grashof number, gβΔT ref L 3/ν 2f
- k s :
-
thermal conductivity of the board material and heat source (W/m K)
- k f :
-
thermal conductivity of air (W/m K)
- L, t :
-
height and thickness of the board, respectively (m)
- L h :
-
height of each of the discrete heat sources (m)
- M, N :
-
number of grids in horizontal and vertical directions, respectively
- N 1 :
-
number of grids up to the trailing edge of the board
- N 2 :
-
total number of grids up to the end of the first heat source
- N 3 :
-
total number of grids up to the start of the second heat source
- N 4 :
-
total number of grids up to the end of the second heat source
- N 5 :
-
total number of grids up to the start of the third heat source
- N RF :
-
radiation–flow interaction parameter, \( \raise0.7ex\hbox{${\sigma T_{\infty } ^{4} }$} \!\mathord{\left/ {\vphantom {{\sigma T_{\infty } ^{4} } {{\left[ {{k_{{\text{f}}} \Updelta T_{{{\text{ref}}}} } \mathord{\left/ {\vphantom {{k_{{\text{f}}} \Updelta T_{{{\text{ref}}}} } {L}}} \right. \kern-\nulldelimiterspace} {L}} \right]}}}}\right.\kern-\nulldelimiterspace} \!\lower0.7ex\hbox{${{\left[ {{k_{{\text{f}}} \Updelta T_{{{\text{ref}}}} } \mathord{\left/ {\vphantom {{k_{{\text{f}}} \Updelta T_{{{\text{ref}}}} } {L}}} \right. \kern-\nulldelimiterspace} {L}} \right]}}$} \)
- P :
-
pressure at any location in the computational domain (Pa)
- Pe L :
-
Peclet number, Re L Pr
- Pr :
-
Prandtl number of air
- q v :
-
volumetric heat generation in each of the discrete heat source (W/m3)
- Re L :
-
Reynolds number, u ∞ L/ν f
- Ri *L :
-
modified Richardson number, gβΔT ref L/u 2∞ or Gr *L /Re 2L
- T :
-
temperature at any location in the computational domain (K or °C)
- T max :
-
maximum temperature in the board (K or °C)
- T ∞ :
-
free stream temperature of air (K or °C)
- u, v :
-
vertical and horizontal components of velocity of air (m/s)
- u ∞ :
-
velocity of air (m/s)
- U :
-
non-dimensional vertical velocity components of air, u/u ∞ or ∂ψ/∂Y
- V :
-
non-dimensional horizontal velocity components of air, v/u ∞ or −∂ψ/∂X
- W :
-
width of the computational domain (m)
- x :
-
vertical distance (m)
- X :
-
non-dimensional vertical distance, x/L
- y :
-
horizontal distance (m)
- Y :
-
non-dimensional horizontal distance, y/L
- α :
-
thermal diffusivity of air (m2/s)
- β :
-
isobaric cubic expansivity of air, \( - \frac{1} {\rho }{\left( {\frac{{\partial \rho }} {{\partial T}}} \right)}_{{\text{p}}} \) (K−1)
- γ :
-
thermal conductance parameter, k f L/k s t
- δ c :
-
convergence criterion, in percentage, \( {\left| {{{\left( {\xi _{{{\text{new}}}} - \xi _{{{\text{old}}}} } \right)}} \mathord{\left/ {\vphantom {{{\left( {\xi _{{{\text{new}}}} - \xi _{{{\text{old}}}} } \right)}} {\xi _{{{\text{new}}}} }}} \right. \kern-\nulldelimiterspace} {\xi _{{{\text{new}}}} }} \right|} \times 100\% \)
- ΔT ref :
-
modified reference temperature difference, q v L h t/k s (K or °C)
- Δx f :
-
height of the board element chosen for energy balance in non-heat source portion (m)
- Δx h :
-
height of the board element chosen for energy balance in the heat source portion (m)
- ε :
-
surface emissivity
- θ :
-
non-dimensional temperature, (T − T ∞)/ΔT ref
- θ max :
-
non-dimensional maximum board temperature
- ν f :
-
kinematic viscosity (m2/s)
- ξ :
-
any dependent variable (ψ, ω or θ) over which convergence is being tested for
- ρ, ρ ∞ :
-
local and characteristic values of fluid density, respectively (kg/m3)
- σ :
-
Stefan–Boltzmann constant (5.6697 × 10−8 W/m2 K4)
- ψ :
-
non-dimensional stream function, ψ′/u ∞ L
- ψ′:
-
stream function (m2/s)
- ω :
-
non-dimensional vorticity, ω′L/u ∞
- ω′:
-
vorticity (s−1)
- cond, x, in:
-
conduction heat transfer into an element along the board
- cond, x, out:
-
conduction heat transfer out of an element along the board
- conv:
-
convection heat transfer from an element
- new, old:
-
values of any variable from the current and previous iterations, respectively
- rad:
-
heat transfer by surface radiation from an element
References
Blasius H (1908) Grenzschichten in Flussigkeiten mit kleiner Reibung. Z Math Phys 56:1, as reported in Chapman AJ Heat Transfer. Macmillan, New York, 1989
Sparrow EM, Gregg JL (1959) Buoyancy effects in forced convection flow and heat transfer. ASME J Appl Mech 81:133–134
Lloyd JR, Sparrow EM (1970) Combined forced and free convection flow on vertical surfaces. Int J Heat Mass Transfer 13:434–438
Wilks G (1973) Combined forced and free convection flow on vertical surfaces. Int J Heat Mass Transfer 16:1958–1964
Ramachandran N, Armaly BF, Chen TS (1985) Measurements and predictions of laminar mixed convection flow adjacent to a vertical surface. ASME J Heat Transfer 107:636–641
Chen TS, Armaly BF, Ramachandran N (1986) Correlations for laminar mixed convection flows on vertical, inclined and horizontal flat plates. ASME J Heat Transfer 108:835–840
Chen TS, Armaly BF, Aung W (1985) Mixed convection in laminar boundary-layer flow. In: Kakac S, Aung W, Viskanta R (eds) Natural convection: fundamentals and applications. Hemisphere, Washington, pp 699–725
Kishinami K, Saito H, Suzuki J, Ali AHH, Umeki H, Kitano N (1998) Fundamental study of combined free and forced convective heat transfer from a vertical plate followed by a backward step. Int J Numer Methods Heat Fluid Flow 8:717–736
Gururaja Rao C, Balaji C, Venkateshan SP (2000) Numerical study of laminar mixed convection from a vertical plate. Int J Transp Phenomena 2:143–157
Zinnes AE (1970) The coupling of conduction with laminar natural convection from a vertical flat plate with arbitrary surface heating. ASME J Heat Transfer 92:528–534
Tewari SS, Jaluria Y (1990) Mixed convection heat transfer from thermal sources mounted on horizontal and vertical surfaces. ASME J Heat Transfer 112:975–987
Hossain MA, Takhar HS (1996) Radiation effect on mixed convection along a vertical plate with uniform surface temperature. Heat Mass Transfer/Waerme Stoffuebertrag 31:243–248
Merkin JH, Pop I (1996) Conjugate free convection on a vertical surface. Int J Heat Mass Transfer 39:1527–1534
Cole KD (1997) Conjugate heat transfer from a small heated strip. Int J Heat Mass Transfer 40:2709–2719
Gururaja Rao C (2004) Buoyancy-aided mixed convection with conduction and surface radiation from a vertical electronic board with a traversable discrete heat source. Numer Heat Transfer Part A 45:935–956
Gururaja Rao C, Balaji C, Venkateshan SP (2001) Conjugate mixed convection with surface radiation from a vertical plate with a discrete heat source. ASME J Heat Transfer 123:698–702
Gosman AD, Pun WM, Runchal AK, Spalding DB, Wolfshtein M (1969) Heat and mass transfer in recirculating flows. Academic Press, New York
Ostrach S (1953) An analysis of laminar free convection flow and heat transfer about a flat plate parallel to the generating body force. NACA Rep.1111, as reported in Chapman AJ Heat Transfer. Macmillan, New York, 1989
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Sawant, S.M., Gururaja Rao, C. Conjugate mixed convection with surface radiation from a vertical electronic board with multiple discrete heat sources. Heat Mass Transfer 44, 1485–1495 (2008). https://doi.org/10.1007/s00231-008-0395-3
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DOI: https://doi.org/10.1007/s00231-008-0395-3