共查询到17条相似文献,搜索用时 109 毫秒
1.
2.
3.
4.
《物理学报》2021,(13)
池沸腾是一种高效的传热方式,目前主要通过刚性固体表面改性强化沸腾传热.本文以乙醇为工质,实验研究了光滑铜表面和液态金属软表面池沸腾传热.发现液态金属软表面可有效降低沸腾起始点(ONB)壁面过热度,饱和沸腾时, ONB壁面过热度从光滑铜表面的约18℃降低到软表面的约6℃,沸腾传热系数最大提高了149%.与光滑铜表面相比,液态金属软表面增加了汽泡核化穴数量,减小了汽泡尺寸,提高了汽泡脱离频率.观察到软表面弹性毛细波和汽泡射流现象.弹性毛细波增强了壁面热边界层热质传递.发现汽泡脱离过程中,汽泡尾部在液态金属薄层内形成残余核化穴,残余核化穴快速长大,与上升的大汽泡聚合,形成汽泡射流现象.弹性毛细波及汽泡射流解释了液态金属软表面强化池沸腾传热的机理. 相似文献
5.
6.
7.
以去离子水为工质,对高为2mm,宽分别为0.3mm、0.6mm、2mm的矩形微槽中的两相传热特性与流动阻力特性进行了实验与理论研究。实验结果表明,三种微槽的饱和沸腾传热系数随着热流密度的增加而增加,并对三种微槽传热系数随热流密度关系的实验数据进行了拟合,得出了实验条件下的传热系数与热流密度的关联式及相同热流密度或者质量流速下槽道尺寸对传热系数的影响;此外,矩形微槽道压降△p随着尺寸的减小而增大。 相似文献
8.
9.
瞬态高热流加热下饱和液氮会发生爆发沸腾,而对于该过程的特殊传热机理因素,目前还没有相关的深入研究和分析。本文基于实验,在总结沸腾传热机理研究成果的基础上,重点分析了饱和液氮爆发沸腾过程中以汽泡群形态实现热量传递的特殊之处,并进行了理论模拟验证。结果表明,汽泡群内部众多汽泡所发生的破裂收缩行为,会释放潜热并形成热流,成为爆发沸腾独特的传热机理影响因素。 相似文献
10.
矩形微槽道饱和沸腾临界热流密度特性 总被引:4,自引:2,他引:2
对矩形微槽中的流动沸腾临界热流密度进行了实验研究。研究CHF随质量流速、进口过冷度和出口干度的增加而出现的变化趋势,以及槽道尺寸对CHF的影响。搭建试验平台,在不同槽道当量直径、较大范围的质量流速和不同进口过冷度条件下,获得以去离子水为工质两相沸腾传热的实验数据。由于常规尺寸槽道CHF预测关联式并不具有普遍性,所以提出了一个适用于微槽道饱和沸腾CHF的预测模型。并通过与该文以及参考文献中实验数据进行对比,验证了该模型的适用性。 相似文献
11.
12.
13.
Experimental results concerning pool film boiling on a wire under the action of an externally imposed electric field are reported. The working fluid was saturated R113 at atmospheric pressure, the heaters were platinum wires of 0.2, 0.3, and 0.6 mm diameter. An electrostatic field of cylindrical geometry was created around the wire by means of a 60-mm-diameter cylindrical cage in order to assess electrohydrodynamic (EHD) effects on boiling. Voltages up to 15 kV d.c. were applied. The results showed that two different film boiling regimes, separated by an additional boiling crisis, can exist in the presence of an electric field. The first regime, at low wire superheat, is strongly influenced by the electric field, showing a remarkable heat transfer enhancement with increasing voltage. The second one, at higher superheat, is weakly dependent on the field strength and almost coincident with the zero field one. The two film boiling regimes are separated by a transition characterized by a hysteresis cycle, similar to the one between nucleate boiling and first film boiling regime. 相似文献
14.
Ultrasound is considered to be an effective active heat transfer enhancement method, which is widely used in various fields. But there is no clear understanding of flow boiling heat transfer characteristics in micro/mini-channels under ultrasonic field since the studies related are limited up to now. In this paper, a novel minichannel heat exchanger with two ultrasonic transducers inside the inlet and outlet plenum respectively is designed to experimentally investigate the impacts of ultrasound on flow boiling heat transfer enhancement in a minichannel heat sink. Flow visualization analyses reveal that ultrasound can promote rapid bubble motion, bubble detachment from heating wall surface and thereby new bubble generation, and decrease the length of confined bubble. Furthermore, the flow boiling experiments are initiated employing working fluid R141b at different ultrasonic parameters (e.g., frequency, power, angle of radiation) and heat flux under three types of ultrasound excitations: no ultrasound (NU), single inlet ultrasound (IU), inlet and outlet ultrasound (IOU). The results indicate that ultrasound has obvious augmentation effects on flow boiling heat transfer even though the intensification effects will be limited with the heat flux increases. The higher ultrasonic power, the lower ultrasonic frequency and the higher ultrasonic radiation angle, the better intensification efficiency. The maximum enhancement ratio of have in the saturated boiling section reaches 1.88 at 50 W, 23 kHz and 45° under the experimental conditions. This study will be beneficial for future applications of ultrasound on flow boiling heat transfer in micro/mini-channels. 相似文献
15.
16.
This article deals with an experimental study of the influence of a DC uniform electric field on the nucleate boiling heat transfer. Electrohydrodynamic (EHD) effects on heat transfer coefficients for dielectric liquids are quantitatively investigated by performing experiments on various liquids with different properties. In these experiments, n-pentane, R-113, and R-123 are used as working fluids and the boiling phenomenon takes place on a horizontal plane copper surface. The experimental results have shown: (1) a threefold increase of nucleate pool boiling heat transfer coefficients, (2) a threefold increase of the critical heat flux (CHF), and (3) the disappearance of the hysteresis phenomenon. For nucleate pool boiling and CHF regimes, heat transfer laws based on dimensionless numbers are proposed. The results obtained by the proposed EHD model are in good agreement with the experimental results. 相似文献