微重力池沸腾传热实验研究

本文实验研究了平板加热面FC-72液体的准稳态池沸腾传热现象,利用地面常重力实验、SJ-8卫星搭载微重力实验等手段,分析了不同重力、压力及过冷度条件下平板加热面上的池沸腾传热特性.微重力条件下,相近压力或过冷度时,传热系数和CHF随过冷度或压力增大而增大.相对常重力,传热曲线明显变缓,沸腾起始时的壁面过热度降低,CHF仅为常重力的40%或更低.     

过冷池沸腾落塔短时微重力实验研究

本文研制了一套控温池沸腾实验设备,利用中国科学院国家微重力实验室落塔开展了短时微重力环境下的过冷池沸腾传热实验研究.加热元件为长30 mm、直径60 μm的铂丝.实验工质为O.1 MPa压力下过冷度为24℃的R113.在地面常重力和落塔短时微重力实验中,观测到核态沸腾和双模态过渡沸腾现象.对核态沸腾,微重力传热效果稍有增强而汽泡形态却呈现出剧烈变化.对双模态过渡沸腾,微重力下膜态沸腾部分有明显收缩,但热流密度值仍比常重力时减小20%.     

微重力准稳态池沸腾中的气泡动力学研究

本文实验研究了微重力条件下的准稳态核态池沸腾现象中的气泡动力学特征及其对传热特性的影响,发现在低过冷度沸腾中,聚合汽泡表面的强烈振荡促进了整个加热面上的核化过程与核态沸腾传热;而高过冷沸腾中,聚合气泡在表面张力作用下呈球状,难以覆盖整个加热表面,导致核态沸腾向膜态沸腾的过度过程表现为"核态沸腾+局部的干斑扩展"现象,相应的传热曲线没有明显转折.微重力条件下池沸腾临界热流随过冷度和压力的增加而升高,与地面结果定性相符.     

微重力下光滑表面上FC-72的池沸腾实验研究

本文利用小尺度光滑芯片(10 mmxl0 mmx0.5 mm),通过控制加热电流方法,在北京落塔进行了持续3.6 s有效微重力时间的过冷池沸腾实验研究.在低热流和中等热流区,微重力条件下可以观察到稳态或准稳态池沸腾现象,传热特性基本维持不变;在中等热流区域,气泡的横向合并会引起合并后的大气泡表面剧烈震荡,进而引发合并大...     

浮升力对管内水过冷流动沸腾传热特性的影响研究

基于已知的2087组水的过冷流动沸腾传热实验数据,通过努塞尔数(Nu)和格拉晓夫数(Gr)的关系探讨了不同流动方向和加热方式下浮升力对过冷流动沸腾传热性能的影响。对上壁面单边加热水平矩形管内过冷流动沸腾传热进行了实验研究。实验结果表明,向上的浮升力阻碍了气泡向流体中的扩散,使得传热恶化。在增加流速、增大压力和减小过冷度的条件下,Nu均随Gr增加,使过冷流动沸腾传热得到强化。     

SOBER-SJ10池沸腾现象天地实验研究

SOBER-SJ10是实践十号科学实验卫星19项科学实验载荷之一,通过局部过热在固定位置预定时刻激发产生气泡,并细致观测空间微重力条件下池沸腾现象中生长气泡热动力学过程与传热特征,来揭示沸腾气泡底部细观流动以及传热特性。利用已完成的7次地面实验、1次在轨阶段空间实验以及3次留轨阶段补充实验相关数据,分析了不同过冷度下地面实验沸腾曲线,并通过对天地实验中的沸腾气泡行为及气泡底部加热面温度等结果的对比分析,探讨了微重力环境对相关过程的影响。     

微重力池沸腾现象中的汽泡行为特性

本文对准稳态加热条件下的微重力核态池沸腾中的汽泡行为特征进行了实验研究,分析了初始核化过程、汽泡数密度、汽泡尺寸及其运动速度等的变化趋势,探讨了过冷度及加热历史等因素对相关特性的影响.实验发现:微重力条件下汽泡生成后沿加热面不停地移动;原生汽泡会聚合形成大汽泡,大汽泡不断捕掠小汽泡而长大,直到大汽泡覆盖整个加热面;汽泡生长速度随过冷度增加而变慢.     

基于遗传算法的SOBER-SJ10池沸腾传热研究

基于遗传算法构建了沸腾过程中加热固壁一维瞬态导热反问题计算方法,采用具有精确解的半无限瞬态导热问题构造了一个校核算例,验证了该算法具有较高的准确度和抗干扰能力,能够准确反演计算沸腾传热瞬态热流密度。基于该算法分析了 SOBER-SJ10地面和空间实验中沸腾传热特性,结果表明微重力环境中单相传热被严重抑制,热流密度远小于地面数值;不同重力条件下核态沸腾传热曲线落在同一位置,显示出低热流密度时核态沸腾传热具有某种重力无关特征;但微重力条件下核态沸腾曲线起始于远低于地面的热流密度,同时在远比地面小的热流密度值时达到临界热流状态,并转变为过渡沸腾模式。     

超声波对池沸腾换热影响

对不同超声强度和辐射距离条件下过冷池沸腾换热特性进行了实验研究.超声波有效强化了沸腾起始段换热,对高热流密度沸腾传热也有一定的强化作用.超声辐射距离越近,强度越大,强化传热效果越好.对单相对流和沸腾起始区传热,超声波强化传热机理为空化作用;高热流密度沸腾时超声波对强化传热的主要机理是声流作用.得到了传热实验关联式.     

微重力下微结构表面强化沸腾换热研究

为了提高航天器中电子器件的冷却效率,本文利用干式腐蚀方法形成方柱微结构,通过控制加热电流方法,在北京落塔进行了持续3.6 s有效微重力时间的过冷FC-72池沸腾强化换热实验研究。研究结果表明:相比光滑表面,方柱微结构表面利用其独立于重力水平的毛细作用力,显著地强化了微重力沸腾换热。     

COUNTERCURRENT FLOODING IN VERTICAL-TO-INCLINED PIPES

Countercurrent flooding data have been obtained using air and water for vertical-to-downwardly inclined pipes containing elbows of varying angles. Experiments were performed with six different test sections, all having an inner diameter of 51 mm and a 1-m-tong vertical tube connected to an inclined or horizontal tube

The flooding data for 112.5° and 135° elbow angles were almost identical and showed that these geometries required the largest gas flow rates for flooding among all the geometries tested. The flooding gas velocities for the 157.5° elbow were slightly less than those of the 112.5° and 135° elbows but greater than those of the vertical pipe without any elbow and vertical-to-horizontal pipes at low to moderate liquid flow rates

In all vertical-to-inclined pipes, flooding was initiated in the inclined section at about 15 to 50 cm downstream of the elbow. Due to the countercurrent flow of gas, the liquid stream just downstream of the elbow became highly agitated and a frothy mixture was carried upstream by gas at flooding. At moderate to high liquid flow rates, the liquid was deflected off at the elbow to form a turbulent, jetlike stream that partially broke up into droplets, These droplets were, at the onset of flooding, entrained and carried over by the gas stream

Comparison of the data with the slugging correlation at low liquid flow rates and with the liquid entrainment/carryover model at high liquid flow rates suggested that these mechanisms are likely responsible for flooding in vertical-to-inclined pipes.     

浸没在多孔介质中的竖直管沸腾换热实验研究

本文对竖直管外填充固体颗粒情况下，蒸馏水和无水乙醇两种工质的池沸腾换热现象进行了实验研究，分析了颗粒直径以及工质热物性对竖直管液池沸腾换热特性，包括沸腾滞后的影响规律，证明了在填充固体颗粒条件下，竖直管的池沸腾换热可以得到一定程度的强化，在低热负荷区，强化效果尤为明显。大颗粒对沸腾滞后现象有较好的缓解作用。在高热负荷区，由于气膜的出现，沸腾机理将有所改变。     

竖直平壁上双组分混合液膜态沸腾换热解析研究

本文应用近似解析方法对双组分混合液在竖直平壁上的膜态沸腾换热进行了理论分析,得到了其平均膜态换热系数的解析计算式,并通过三种典型的双组分混合液例证了传质过程对换热的影响。     

光管及窄环隙流道池沸腾换热实验研究

本文在常压下以水为工质,对管外及窄环隙流道池沸腾换热进行了可视化实验,结果表明：汽泡扰动并不是沸腾换热系数高的主要原因,液体过冷使核沸腾的换热能力降低,窄隙流道内的沸腾换热机理与普通的大容积沸腾没有明显区别。文中还根据观察和测量到的结果对一些换热现象重新进行了解释。     

微尺度水平单管内流动沸腾特性实验研究

对非共沸混合工质R134a/R32(75/25)在水平微尺度管道内的流动沸腾换热实验结果进行了分析和讨论,以探究微细通道内流动沸腾换热的主导机制。对影响其换热的多种因素(热流密度、质量流量和质量干度)进行了分析,实验得出,当质量干度较低时,热流密度和质量流量共同控制着微尺度管内的换热方式,当热流密度的影响占主导地位时,管道内的换热以核态沸腾为主;当质量流量的影响占主导地位时,管道内的换热以强制对流为主。     

NUCLEATE POOL BOILING HEAT TRANSFER OF BINARY MIXTURES WITH DIFFERENT BOILING RANGES

The nucleate pool boiling heat transfer data on a smooth flat surface were measured for three binary mixtures of HC600a/HFC134a, HC600a/HC290, and HC600a/HFC23. Much effort was made to investigate the influence of the boiling range on the pool-boiling heat transfer performance. From the experimental results, the HC600a/HFC23 mixture with a wide boiling range showed lower heat transfer coefficients (HTCs) than the mixture with a narrow boiling range such as HC600a/HFC134a and HC600a/HC290 systems. The measured data were also compared with the results predicted by five well-known correlations. It can be found that the average deviation is less than 25% for mixtures with narrow boiling ranges, but a larger deviation for mixtures with wide boiling ranges.     

PTFE疏水修饰法消除多孔表面的沸腾迟滞现象

微纳多孔结构表面在提高沸腾传热性能的同时,通常也会伴随着沸腾迟滞现象出现.以底部树林状阵列结构、上部蜂窝状微纳双尺度多孔结构为基础的双层多孔表面在展示出良好性能的同时,也出现了沸腾迟滞现象。本文通过电泳沉积PTFE修饰的方法,降低多孔表面成核壁面过热度,从而基本消除双层多孔表面的沸腾迟滞效应。另外,修饰后的双层多孔表面的CHF和最大HTC与未修饰的双层多孔表面相比提高了20%和19%;和光滑铜表面相比,CHF提高了97%,HTC提高了400%,展现出优异的沸腾传热性能.     

微槽结构和工质对槽内流动沸腾的影响

本文报道实验测试甲醇等低沸点工质在微槽内流动沸腾特性的结果，并对所呈现的起始沸腾区有明显壁温回落等现象作出分析，从而在一定程度上揭示出微型槽道和工质本身特性对流动沸腾特性的影响。     

The effect of oxide layer in case of novel coolant spray at very high initial surface temperature

The significant reduction of Leidenfrost effect during the cooling of high carbon steel plate by different potential cooling methodologies does not assure their successful implementation in the fast quenching of high carbon steel plate due to the formation of oxide layer of comparatively low thermal conductivity on the quenching surface. Therefore, the role of oxide layer in case of different potential cooling methodologies needs to be addressed. In the present study, the effect of oxide layer on heat transfer rate in case of upward, downward, and both upward and downward facing spray with additives has been investigated by conducting and comparing the heat transfer cooling data of an AISI 1020 plate with the AISI 304 plate. The comparison clearly depicts that the formation of oxide layer during cooling significantly hinders the heat transfer rate in nucleate boiling regime; however, the reverse phenomenon is observed in transition boiling regime. Among all the coolants, the least effect of oxide layer on enhancement is obtained in case of NaCl (0.4 M)-added water spray due to the deposition of salt on the evaporating surface. The X-ray diffraction analysis and the thickness of the formed oxide layer clearly assert that the coolant depicting minimum oxidation characteristic is preferred.

Abbreviations: AISI: American iron and steel institute; OES: Optical emission spectrophotometer; CHF: Critical heat flux, MW/m²; IHF: Initial heat flux, MW/m²; T_CHF: Temperature at which CHF is achieved, °C; Fps: Frames per second; XRD: X-Ray diffraction; k₁: Thermal conductivity of steel plate, W/m °C; k₂: Thermal conductivity of oxide layer, W/m °C; k₃: Thermal conductivity of coolant, W/m °C; X: x-axis, mm; Y: y-axis, mm; Z: z-axis, mm     

Subcooled Flow Boiling Heat Transfer to Water and Ethylene Glycol/Water Mixtures in a Bottom-heated Tube

Subcooled flow boiling heat transfer experiments were performed with water and ethylene glycol/water mixtures at five flow velocities and four fluid inlet temperatures. Both turbulent flow and laminar flow were tested in a special test facility with its experimental test section heated from the bottom surface only. Boiling curves and subcooled flow boiling heat transfer coefficients of the tested fluids were determined from the experimental measurements. Predictive correlations of the subcooled flow boiling heat transfer coefficients were developed based on the experimental data. Comparisons are presented of wall temperatures between the experimental measurements and the correlation predictions.