新型相分離冷凝器相變傳熱強(qiáng)化機(jī)理研究

徐進(jìn)良

摘 要：該研究針對(duì)有機(jī)工質(zhì)朗肯循環(huán)系統(tǒng)中的關(guān)鍵部件冷凝器，創(chuàng)新性地提出了流型調(diào)控的新概念，通過(guò)采用相分離概念，在冷凝管內(nèi)插入柱狀金屬絲網(wǎng)，在毛細(xì)力的作用下，液體被自動(dòng)吸入到金屬網(wǎng)內(nèi)，而氣相在管內(nèi)壁和金屬網(wǎng)之間的環(huán)形間隙內(nèi)流動(dòng)，達(dá)到了流型調(diào)控的目的。該研究通過(guò)無(wú)相變空氣-水兩相流型調(diào)控實(shí)驗(yàn)和數(shù)值研究發(fā)現(xiàn)：（1）水平光滑管內(nèi)的分層流，經(jīng)過(guò)新型結(jié)構(gòu)管后，液體被全部吸入金屬絲網(wǎng)而導(dǎo)出，氣體則全部保留在了環(huán)形間隙內(nèi)；（2）水平光滑管內(nèi)的間隙流，經(jīng)過(guò)新型結(jié)構(gòu)管后，部分液體被吸入金屬絲網(wǎng)而導(dǎo)出，氣泡則在環(huán)形間隙內(nèi)轉(zhuǎn)變?yōu)轳R鞍形，從而大大增大了氣相與管內(nèi)壁的接觸面積，形成大面積薄液膜傳熱，同時(shí)氣相被加速，強(qiáng)化了對(duì)流傳熱；（3）垂直光滑管內(nèi)的間歇流，經(jīng)過(guò)新型結(jié)構(gòu)管后，由于絲網(wǎng)表面張力作用，氣彈進(jìn)入環(huán)隙區(qū)域，形成拉長(zhǎng)的環(huán)形氣彈，氣彈與管內(nèi)壁的接觸面積變大，液膜厚度大幅減薄，同時(shí)氣彈上升速度大幅提高，引起環(huán)隙區(qū)域和核心區(qū)域內(nèi)的流體通過(guò)網(wǎng)孔面進(jìn)行強(qiáng)烈的質(zhì)量與動(dòng)量的交換并在核心區(qū)域產(chǎn)生自維持脈動(dòng)流，以上因素均有利用提高設(shè)備換熱性能。 該研究通過(guò)光管與內(nèi)插絲網(wǎng)管的R123水平管內(nèi)冷凝對(duì)比實(shí)驗(yàn)以及光管與內(nèi)插銅粉燒結(jié)管的R245fa傾斜內(nèi)冷凝對(duì)比實(shí)驗(yàn)研究，得出：不銹鋼絲網(wǎng)管和銅粉燒結(jié)管均通過(guò)流型調(diào)控強(qiáng)化了管內(nèi)冷凝，實(shí)驗(yàn)工況范圍內(nèi)，最大傳熱強(qiáng)化比達(dá)兩倍以上，綜合評(píng)價(jià)因子達(dá)到1.7。

關(guān)鍵詞：冷凝器 相分離 金屬絲網(wǎng) 流型調(diào)控 強(qiáng)化換熱

Research on Heat Transfer Enhancement Mechanism of Phase Separation Condenser

Xu Jinliang

（North China Electric Power University）

Abstract：For enhancing the heat transfer performance of the condenser in the organic Rankine cycle system， a flow pattern modulation concept was proposed by our group. A mesh cylinder is suspended in the heat transfer tube. Based on the experimental and numerical researches on the air-water two-phase flow pattern modulation process， we can obtain the following conclusions. （1） For the stratified flow in the horizontal tube， all liquid can be captured by the mesh cylinder to form the “gas-floating-liquid” mode. Gas is kept in the annular region. （2） For the intermittent flow pattern in the horizontal tube， the slug bubbles are prevented from entering the mesh cylinder thus they flow in the annular region to form the saddle bubbles. The condensation can be significantly enhanced by the following two mechanisms： the significantly increased contact area between the tube inner wall and the vapor phase； the increased moving speed of the saddle bubble in the annular region. （3） For the intermittent flow pattern in the vertical tube， the slug bubble cannot completely breakthrough the mesh pores， forcing the bubble flowing in the annular region to form the elongated-ring-slug-bubble. It was found that the modulated liquid film thickness can be decreased largely； the modulated bubble traveling velocity can be doubled， causing the increased liquid velocity and velocity gradient in the annular region to weaken the fluid boundary layer； the significantly increased bubble traveling velocity in the annular region promotes the mass and momentum exchange between the annular region and the core region， and yields the self-sustained pulsating flow in the core region. The above factors are benefit for the performance improvement of the heat transfer facilities. R123 condensation performance in a horizontal tube compared with that in a tube with a mesh cylinder insert and R245fa condensation performance in a horizontal tube compared with that in a tube with sintered copper powder cylinder insert were investigated experimentally. Conclusions were drawn that condensation heat transfer can be augmented considerably by flow pattern modulation in a tube inserted by empty cylinder made up of mesh screen or sintered copper powder. The heat transfer can be enhanced more than two times of that in a conventional smooth tube for the entire experimental conditions， where the performance factors are about 1.7.

Key Words：Condenser； Phase separation； Metallic mesh screen； Flow pattern modulation； Heat transfer enhancement

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