coefficient of convective heat transfer造句
例句與造句
- Normally , coefficient of convective heat transfer is gotten through experiments which is heating testing tube by electricity and computed through newton cooling law
通常,對流換熱系數(shù)是在實驗中以電加熱試驗管壁面后根據(jù)牛頓冷卻定律計算得來的。 - At the same time , we suggest a correction factor to the before coefficient of convective heat transfer formula at the second boundary condition
然后研究平均對流換熱系數(shù)在電加熱邊界條件和傳熱邊界條件下的區(qū)別,同時提出對以往在電加熱條件下所得出的換熱系數(shù)經(jīng)驗式的修正。 - So if there is any difference of coefficient of convective heat transfer between this two boundary condition ? both numerical simulation and experiment were adopted to research ducted heat convection
探討這兩種邊界條件下管內(nèi)外的對流換熱系數(shù)的差別及相應(yīng)的對應(yīng)關(guān)系對于換熱設(shè)備的設(shè)計具有重要的意義。 - Fist we resarch local wall temperature ouside and inside of tube , local fluid temperature inside and outside of tube , local heat flux inside and outside of tube , local coefficient of convective heat transfer inside and ouside of tube along the tube axial direction
首先研究在這兩種情況下管內(nèi)(外)壁溫、管內(nèi)(外)流溫、管內(nèi)(外)壁面局部熱流密度、管內(nèi)(外)局部對流換熱系數(shù)沿管子軸向的變化。 - The end show that coefficient of convective heat transfer at thermal boundary condition is higher than that at definite heat flux boundary condition . if according to dimensionless equation of heat convection , nu number of the latter almost is mutiplied 1 . 47 times of the formal , but the coefficient of convective heat transfer in tube between this two condition is almost equal
研究結(jié)果表明:在實驗室中電加熱方式得到的管外對流換熱系數(shù)低于工程中傳熱條件下的管外對流換熱系數(shù),若按傳熱準(zhǔn)則式關(guān)系,后者的努謝爾特數(shù)約為前者的1 . 4倍;而管內(nèi)的對流換熱系數(shù)在兩種邊界條件下的差別不大。 - It's difficult to find coefficient of convective heat transfer in a sentence. 用coefficient of convective heat transfer造句挺難的
- In this condition heat convection inside and outside of tube are coupled . coefficient of convective heat transfer inside and outside of tube gotten through such way compare with coefficient of convective heat transfer inside and outside of tube gotten through by electricity . for comparability between this two condition , the average heat flux on the tube must be equal for this two condition
這種情況下管內(nèi)外對流換熱是藕合的,得到的管內(nèi)外對流換熱系數(shù)分別與電加熱管道壁面的邊界條件下管內(nèi)和管外流動的對流換熱系數(shù)相對比,為了使他們具有可比性,我們規(guī)定在這兩種邊界條件下通過管子的平均熱流密度相等。
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