Measurement of Heat Transfer for Water Flow in Sintered Porous Channels

碩士 === 國立清華大學 === 動力機械學系 === 82 === A study of non-Darcian forced convection in an asymmetric heating sintered porous channel was carry out to investigate the feasibility of using this channel as a heat sink for high performance forced wate...

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Bibliographic Details
Main Authors: Wang, Chau Hua, 王朝華
Other Authors: Hwang, Guang Jyh
Format: Others
Language:en_US
Published: 1994
Online Access:http://ndltd.ncl.edu.tw/handle/46454698174732869000
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Summary:碩士 === 國立清華大學 === 動力機械學系 === 82 === A study of non-Darcian forced convection in an asymmetric heating sintered porous channel was carry out to investigate the feasibility of using this channel as a heat sink for high performance forced water cooling in microelectronics. This paper presents the results of heat transfer measurement for two 5×5×1 cm porous channels with sintered bronze beads of d=0.72 and 1.59 mm. The local wall temperature distribution, inlet and outlet pressures and temperatures , and heat transfer coefficients were measured for heat fluxes between 2 and 9 W/c ㎡, and with water velocity ranging from 0 to 11.7 cm/s. The measurement covers the data in both the thermal entrance and thermal fully developed regions. The main objective of the present study is to examine the effects of the particle Reynolds number, the Peclet number, and the ratio of channel height to particle diameter on the local Nusselt number. In the thermal developing region, the results show that the local heat transfer coefficients increase with the decrease in the particle size and the increase in the fluid velocity, but decrease with the increase in the axial distance before reaching its fully developed value. The high conductivity porous channel enchances the heat transfer and the maximum wall temperature could be reduced drastically. For example, the forced water cooling can be extended upto 0.25—4 W/c㎡℃ by a porous heat sink and maintaining a maximum wall temperature less than 45℃. But for forced air cooling, the heat transfer coefficents are about from 0.01 to 0.5 W/c㎡℃。