A way to explain the thermal boundary effects on laminar convection through a square duct

Liangbi WANG, Xiaoping GAI, Kun HUANG, Yongheng ZHANG, Xiang YANG, Xiang WU

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PDF(771 KB)
Front. Energy ›› 2010, Vol. 4 ›› Issue (4) : 496-506. DOI: 10.1007/s11708-010-0020-2
RESEARCH ARTICLE
RESEARCH ARTICLE

A way to explain the thermal boundary effects on laminar convection through a square duct

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Abstract

A way using the reformulation of the energy conservation equation in terms of heat flux to explain the thermal boundary effects on laminar convective heat transfer through a square duct is presented. For a laminar convection through a square duct, it explains that on the wall surface, the velocity is zero, but convection occurs for uniform wall heat flux (UWHF) boundary in the developing region due to the velocity gradient term; for uniform wall temperature (UWT) boundary, only diffusion process occurs on the wall surface because both velocity and velocity gradient do not contribute to convection; for UWHF, the largest term of the gradient of velocity components (the main flow velocity) on the wall surface takes a role in the convection of the heat flux normal to the wall surface, and this role exists in the fully developed region. Therefore, a stronger convection process occurs for UWHF than for UWT on the wall surface. The thermal boundary effects on the laminar convection inside the flow are also detailed.

Keywords

convective transport / heat transfer / mass transfer / laminar flow / thermal boundary effects

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Liangbi WANG, Xiaoping GAI, Kun HUANG, Yongheng ZHANG, Xiang YANG, Xiang WU. A way to explain the thermal boundary effects on laminar convection through a square duct. Front Energ Power Eng Chin, 2010, 4(4): 496‒506 https://doi.org/10.1007/s11708-010-0020-2

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Acknowledgements

This work is supported by the National Natural Science Foundation of China (Grant No. 50876040)
Notation
athermal diffusivity/(m2·s-1)
C combined with other symbol means cross-averaged value of this symbol
cpspecific heat capacity/(kJ·kg-1·K-1)
dhhydraulic diameter/m
ei,jsecond order tensor or velocity gradient/s-1
ffriction factor
hheat transfer coefficient/(W·m-2·K-1)
BoldItalic,BoldItalic,BoldItalicunit vector respecting to x, y, z direction
nnormal direction/m
NuNusselt number
W combination terms in heat flux convection equation/(W·m-2·s-1)
x, y, z coordinator axes/m
lthermal conductivity/(W·m-1·K-1)
mviscosity/(kg·m-1·s-1)
rdensity/(kg·m-3)
Ñoperator/m-1
pstatic pressure/(N·m-2)
qcomponents of heat flux vector/(W·m-2)
BoldItalicvector heat flux/(W·m-2)
Scombined with other symbol means span-averaged value of this symbol
SWspan averaged value of W /(W·m-2·s-1)
ttime/s
T temperature/K
Subscript
u, v, wcomponents of velocity vector/(m·s-1)
BoldItalicvelocity vector/(m·s-1)
bulkcross averaged value
c-x, c-y, c-zterms in heat flux equation related to velocity
e-x, e-y, e-zterms in heat flux equation related to velocity gradient
locallocal value
sspan averaged value
x, y, zalong x, y, z direction, respectively
wwall

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2014 Higher Education Press and Springer-Verlag Berlin Heidelberg
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