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研究生:王朝華
研究生(外文):Wang, Chau Hua
論文名稱:多孔燒結介質槽中水流之熱傳量測
論文名稱(外文):Measurement of Heat Transfer for Water Flow in Sintered Porous Channels
指導教授:黃光治
指導教授(外文):Hwang, Guang Jyh
學位類別:碩士
校院名稱:國立清華大學
系所名稱:動力機械學系
學門:工程學門
學類:機械工程學類
論文種類:學術論文
論文出版年:1994
畢業學年度:82
語文別:英文
論文頁數:45
中文關鍵詞:多孔燒結介質水流熱傳量測
外文關鍵詞:Sintered Porous ChannelsWater FlowHeat Transfer
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本文針對多孔矩形槽中非達西強制熱對流的熱傳效應進行實驗研究,並探
討在電子裝備冷卻方面的應用。實驗是以水及5×5×1公分加熱的燒結銅
粒槽來進行,其中燒結銅粒的平均顆粒直徑共有0.72及1.59 ㎜兩種尺寸
。所量測的參數包括沿水流流動方向的局部壁溫、進出口處的壓力差和溫
度、及所對應的局部熱傳係數。實驗的邊界狀況是上板加熱且另外三邊絕
熱,所加的等熱通量為2—9 W/c㎡,水流速度介於0和11.7cm/s之間,量
測結果包含熱進口區及全展區。實驗的主要目的在於瞭解不同的顆粒直徑
、雷諾數、等熱通量、及軸向位置下對於熱傳效果的影響。實驗結果顯示
:當在較大的雷諾數與較小的顆粒直徑時,熱進口區的局部熱傳係數有較
高的值,並隨著軸向位置的增加而遞減,至某一距離以後便趨向一常數值
而達到全展的狀況。由於高熱傳係數多孔介質的存在,使得局部熱傳率提
高並大大地降低局部壁溫。本實驗中對流熱傳係數可從 0.25提高至4 W/c
㎡℃,若以空氣為工作流體,則對流熱傳係數的範圍約為0.01—0.5 W/c
㎡℃。

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㎡℃。

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