TY - GEN
T1 - Inaccuracy of heat transfer characteristics of a metal duct neglecting heat radiation effect in ambient air
AU - Wong, King Leung
AU - Chen, Wen Lih
AU - Chiu, Yung Chin
N1 - Copyright:
Copyright 2012 Elsevier B.V., All rights reserved.
PY - 2012
Y1 - 2012
N2 - A heat radiation equation contains 4 th exponential order of temperature which makes mathematics analysis complicated and time-consumption. Most heat transfer experts and scholars believe, based on their own experiences, that the heat radiation effect can be ignored in situations of small temperature difference between duct surfaces and surroundings. This paper studies in detail for complete heat transfer characteristics of a circular duct with heat radiation effect taken into account. It is found that, in some practical conditions, the heat radiation effect can not be ignored especially in cases of lower ambient convection heat coefficients and larger surface emissivities, as well as the smaller the duct size and/or the greater the duct conductivity and/or internal fluid convection coefficients, even though the temperature-difference between inner and outer fluid-temperatures of duct is low to 1 °C. It is found that the conventional LMTD method (ignoring heat radiation) cannot be applied to calculate the total heat transfer rate of a single-duct heat exchanger located in ambient air, such as condenser and evaporator.
AB - A heat radiation equation contains 4 th exponential order of temperature which makes mathematics analysis complicated and time-consumption. Most heat transfer experts and scholars believe, based on their own experiences, that the heat radiation effect can be ignored in situations of small temperature difference between duct surfaces and surroundings. This paper studies in detail for complete heat transfer characteristics of a circular duct with heat radiation effect taken into account. It is found that, in some practical conditions, the heat radiation effect can not be ignored especially in cases of lower ambient convection heat coefficients and larger surface emissivities, as well as the smaller the duct size and/or the greater the duct conductivity and/or internal fluid convection coefficients, even though the temperature-difference between inner and outer fluid-temperatures of duct is low to 1 °C. It is found that the conventional LMTD method (ignoring heat radiation) cannot be applied to calculate the total heat transfer rate of a single-duct heat exchanger located in ambient air, such as condenser and evaporator.
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U2 - 10.4028/www.scientific.net/AMR.516-517.322
DO - 10.4028/www.scientific.net/AMR.516-517.322
M3 - Conference contribution
AN - SCOPUS:84861688936
SN - 9783037854150
T3 - Advanced Materials Research
SP - 322
EP - 327
BT - Electrical Power and Energy Systems
T2 - 1st International Conference on Energy and Environmental Protection, ICEEP 2012
Y2 - 23 June 2012 through 24 June 2012
ER -