Abstract

The continuous, one-dimensional kernel function in a rectangular duct subject to forced convection with air was experimentally estimated using liquid crystal thermography techniques. Analytical relationships between the kernel function for internal flow and the temperature distribution resulting from a known heat flux distribution were manipulated to accomplish this objective. The kernel function in the hydrodynamically fully developed region was found to be proportional to the streamwise temperature gradient resulting from a constant heat flux surface. In the hydrodynamic entry region of the rectangular duct, a model for the kernel function was proposed and used in its experimental determination. The kernel functions obtained by the present work were shown to be capable of predicting the highly nonuniform surface temperature rise above the inlet temperature resulting from an arbitrary heat flux distribution to within the experimental uncertainty. This is better than the prediction obtained using the analytically derived kernel function for turbulent flow between parallel plates, and the prediction obtained using the conventional heat transfer coefficient for constant heat flux boundary conditions. The latter prediction fails to capture both the quantitative and qualitative nature of the problem. The results of this work are relevant to applications involving the thermal management of nonuniform temperature surfaces subject to internal convection with air, such as board-level electronics cooling. Reynolds numbers in the turbulent and transition range were examined.

1.
Kays
,
W. M.
, and
Crawford
,
M. E.
, 1980,
Convective Heat and Mass Transfer
, 2nd ed.,
McGraw-Hill
, New York.
2.
Sellars
,
J. R.
,
Tribus
,
M.
, and
Klein
,
J. S.
, 1956, “
Heat Transfer to Laminar Flow in a Round Tub or Flat Conduit—The Graetz Problem Extended
,”
Trans. ASME
0097-6822,
78
, pp.
441
448
.
3.
Hatton
,
A. P.
, and
Quarmby
,
A.
, 1963, “
The Effect of Axially Varying and Unsymmetrical Boundary Condition on Heat Transfer With Turbulent Flow Between Parallel Plates
,”
Int. J. Heat Mass Transfer
0017-9310,
33
, pp.
2659
2670
.
4.
Moffat
,
R. J.
, 1998, “
What’s New in Convective Heat Transfer?
,”
Int. J. Heat Fluid Flow
0142-727X,
19
, pp.
90
101
.
5.
Crittenden
,
P. E.
, and
Cole
,
K. D.
, 2002, “
Fast-Converging Steady-State Heat Conduction in a Rectangular Parallelepiped
,”
Int. J. Heat Mass Transfer
0017-9310,
45
, pp.
3585
3596
.
6.
Anderson
,
A. M.
, and
Moffat
,
R. J.
, 1992, “
The Adiabatic Heat Transfer Coefficient and the Superposition Kernel Function: Part 1—Data for Arrays of Flatpacks for Different Flow Conditions
,”
ASME J. Electron. Packag.
1043-7398,
114
(
1
), pp.
14
21
.
7.
Anderson
,
A. M.
, and
Moffat
,
R. J.
, 1992, “
The Adiabatic Heat Transfer Coefficient and the Superposition Kernel Function: Part 2—Modeling Flatpack Data as a Function of Channel Turbulence
,”
ASME J. Electron. Packag.
1043-7398,
114
(
1
), pp.
22
28
.
8.
Hacker
,
J. M.
, and
Eaton
,
J. K.
, 1996, “
Measurements of Heat Transfer in Separated and Reattaching Flow With Spatially Varying Thermal Boundary Conditions
,”
Int. J. Heat Fluid Flow
0142-727X,
18
, pp.
131
141
.
9.
Batchelder
,
K. A.
, and
Eaton
,
J. K.
, 2001, “
Practical Experience With the Discrete Green’s Function Approach to Convective Heat Transfer
,”
ASME J. Heat Transfer
0022-1481,
123
(
1
), pp.
70
76
.
10.
Khon’kin
,
A. D.
, 2000, “
The Taylor and Hyperbolic Models of Unsteady Longitudinal Dispersion of a Passive Impurity in Convection-Diffusion Processes
,”
J. Appl. Math. Mech.
0021-8928,
64
(
4
), pp.
607
617
.
11.
Bokota
,
A.
, and
Iskierka
,
S.
, 1997, “
Numerical Simulation of Transient and Residual Stresses Caused by Laser Hardening of Slender Elements
,”
Comput. Mater. Sci.
0927-0256,
7
, pp.
366
376
.
12.
Mitrovic
,
B. M.
,
Le
,
P. M.
, and
Papavassilious
,
D. V.
, 2004, “
On the Prandtl or Schmidt Number Dependence of the Turbulent Heat or Mass Transfer Coefficient
,”
Chem. Eng. Sci.
0009-2509,
59
(
3
), pp.
543
555
.
13.
Mukerji
,
D.
,
Eaton
,
J. K.
, and
Moffat
,
R. J.
, 2004, “
Convective Heat Transfer Near One-Dimensional and Two-Dimensional Wall Temperature Steps
,”
ASME J. Heat Transfer
0022-1481,
126
(
2
), pp.
202
210
.
14.
Simonich
,
J. C.
, and
Moffat
,
R. J.
, 1982, “
New Technique for Mapping Heat Transfer Coefficient Contours
,”
Rev. Sci. Instrum.
0034-6748,
53
(
5
), pp.
678
683
.
15.
Baughn
,
J. W.
,
Takahashi
,
R. K.
,
Hoffman
,
M. A.
, and
McKillop
,
A. A.
, 1985, “
Local Heat Transfer Measurements Using an Electrically Heated Thin Gold-Coated Plastic Sheet
,”
ASME J. Heat Transfer
0022-1481,
107
(
4
), pp.
953
959
.
16.
Farina
,
D. J.
,
Hacker
,
J. M.
,
Moffat
,
R. J.
, and
Eaton
,
J. K.
, 1994, “
Illuminant Invariant Calibration of Thermochromic Liquid Crystals
,”
Exp. Therm. Fluid Sci.
0894-1777,
9
(
1
), pp.
1
12
.
17.
Moffat
,
R. J.
, 1982, “
Contributions to the Theory of Single-Sample Uncertainty Analysis
,”
ASME J. Fluids Eng.
0098-2202,
104
, pp.
250
260
.
You do not currently have access to this content.