共查询到17条相似文献,搜索用时 187 毫秒
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核态沸腾换热在传热传质方面有着重要的作用,其发生机理和传热传质过程仍是研究的重点。随着实验手段的提高,微液层模型得到了广泛的关注。通过对微液层中传热传质的分析,建立了微液层厚度与热流密度和气化率之间的关系。利用界面扩散法对汽液相界面进行追踪,并在汽泡与加热壁面之间构建微液层模型,研究在核态沸腾条件下,微液层的变化对汽泡生长和加热壁面温度分布的影响。结果表明,数值模拟得到的汽泡生长过程和加热壁面温度分布与实验结果吻合得很好,初步验证了模型的正确性。并通过数值模拟,进一步分析了汽泡生长过程中微液层、干性区域和汽泡底部半径的变化规律以及壁面温度的分布情况。 相似文献
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一般在沸腾传热实验中壁面的加热方式有电加热和流体加热两种,流体加热方式下的沸腾传热研究进行得很少.在水加热条件下,对水在竖直环形流道内欠热流动沸腾时的气泡行为进行了可视化研究.环隙宽度为5mm和3mm两种,质量流速分别为16.8~55.3kg/(m2·s)和15.3~62.1kg/(m2·s).可视化实验结果表明:在贴近壁面的区域存在气泡运动层,大部分气泡在气泡运动层内运动.在宽度为3mm的流道中,气泡在脱离壁面前一般会滑动;滑动距离不超过2~3倍气泡直径,并且存在反复胀缩的现象.5mm流道内的气泡则较少发生滑动,往往在脱离壁面后会被弹回壁面.气泡的滑动和离开壁面后又返回壁面的运动方式是沸腾具有高强度传热能力的原因之一. 相似文献
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铬(Cr)涂层锆合金包壳是最有前途的耐事故燃料(ATF)的新型包覆材料之一,对其表面的气泡动力学进行研究有助于评估是否具有更好的传热性能。在常压下的Cr涂层锆合金包壳池式沸腾实验装置中对不同工艺方法下制备的Cr涂层锆合金包壳进行实验,研究了粗糙度等表面状态对气泡产生、长大以及脱离等气泡行为的影响。结果表明,气泡接触角与Cr涂层表面粗糙度有关,粗糙度越大,表面气泡接触角越小;不同涂层工艺下制备的4种Cr涂层锆合金包壳样件表面的气泡脱离直径范围为1.256~1.446 mm,气泡脱离频率范围为29.99~50.97 Hz;气泡脱离直径与粗糙度呈负相关,脱离频率与粗糙度呈正相关;气泡脱离直径预测模型与实验数据之间的偏差为±6%,脱离频率预测模型与实验数据之间的偏差为±3%。 相似文献
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竖直矩形窄缝通道内近壁汽泡生长和脱离研究 总被引:1,自引:1,他引:0
可视化研究窄缝通道内汽泡生长和脱离对于揭示窄缝通道内的沸腾传热机理具有重要意义。本文采用高速摄影仪从宽面和窄面可视化观察了常压条件下矩形窄缝通道内汽泡核化生长和脱离规律。研究结果表明,汽泡在核化点生长时,汽泡底部与加热面存在一小的接触面,总体而言,汽泡在生长过程中基本呈球状。在相同热工参数下,不同核化点处汽泡生长规律基本相同,但汽泡脱离直径相差较大。窄缝通道内汽泡生长速率小,脱离时间较长,可采用修正的Zuber公式预测窄缝通道内汽泡生长直径。在同一拍摄窗口内,统计分析了热工参数对汽泡平均脱离直径的影响规律。随热流密度的增加,汽泡平均脱离直径减小;随入口欠热度的增加,汽泡平均脱离直径减小;随主流速度的增加,汽泡平均脱离直径减小。 相似文献
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To explore the mechanism of boiling bubble dynamics in narrow channels, two types of channels are investigated which have I- and Z-shaped with width of 2 mm. Using VOF model and self-programming, the whole flow field is simulated with two different kinds of media, namely, water and ethanol. The influence of wall contact angle on the process of bubble generating and growth is studied, and the relationship between different channel shapes and the pressure drop is also investigated taking into account the effects of gravity, viscosity, surface tension and wall adhesion. The bubble generation, growth and departure processes are analyzed through numerical simulation and self-programming, and the influence of interface movements and changes on internal pressure difference and average surface heat transfer coefficient is investigated by using geometry reconstruction and interface tracking. It is found that wall contact angle has a great influence on the morphology of bubble. The smaller the wall contact angles are, the more round the bubbles are, and the less time the bubbles take to depart from the wall. The variation of contact angle also has effect upon the heat transfer coefficient. The greater the wall contact angle is, the larger the bubble-covered area is, thus the wall thermal resistance gets higher, and bubble nucleation is suppressed, and the heat transfer coefficient becomes lower. The role of surface tension in the process of boiling heat transfer is much more important than the gravity in narrow channels. The generation of bubbles dramatically disturbs the boundary layer, and the bubble bottom micro-layer can enhance the heat transfer. The heat transfer coefficient of Z-shaped channels is larger than that of I-shaped ones, while the pressure drop of the former is obviously higher. In addition, surface tension and viscosity significantly impact the pressure drop of boiling system, and different specific heat and boiling point values result in different heat transfer coefficients. The simulation results in this paper match well with the experimental data revealed in other sources, both show that the heat transfer coefficient of water is higher than that of ethanol and Z-shaped channels have better heat transfer capability. 相似文献
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In this study, regression analysis on the thermal properties of Al2O3/H2O nanofluids was made firstly. The growth and departure of a single bubble behavior in Al2O3/H2O nanofluid and pure water flow boiling process were then numerically simulated by an improved Moving Particle Semi-implicit method in different flow boiling conditions. The results indicate that the bubble in Al2O3/H2O nanofluids grows faster and the bubble departure frequency of Al2O3/H2O nanofluids is greater than that in pure water. The flow boiling heat flux is also improved by dispersing nanoparticles of Al2O3/H2O in pure water. This work initially reveals that nanofluids can enhance flow boiling heat transfer from the point of view of bubble dynamics behavior. The effects of nanoparticle concentrations and diameters of Al2O3/H2O nanofluids on the bubble behavior were also investigated and compared under the same flow conditions. It is found that the increasing of nanoparticle volume concentration may increase the bubble departure frequency and departure diameter, while the increasing rates of departure frequency and departure diameter are lessened with the increasing of nanoparticle volume concentration. It is suggested that the suitable nanoparticle volume concentration of nanofluid for flow boiling heat transfer enhancement should not be too large, especially regarding the negative effect of flow resistance increase due to the increasing of nanoparticle volume concentration. The interesting finding is that in the same nanoparticle volume concentration condition, the bubble departure frequency for the nanofluid with nanoparticle diameter of 29 nm shows a maximum value. The increasing of nanoparticle diameter leads to the decreasing of bubble departure diameter. It is boldly to predict that an optimal nanoparticle diameter range between 20 and 38 nm should be beneficial to flow boiling heat transfer enhancement of Al2O3/H2O nanofluids. 相似文献
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Visual experimental study focusing on bubble growth and departure behaviors in a narrow rectangular channel was carried out in this paper. Deionized water was used as working fluid, and the experiment was performed at atmospheric pressure. The cross section of the narrow rectangular channel is 2 mm × 8 mm. A high speed digital camera was applied to capture the behaviors of bubble growth and bubble departure from the nucleation site. The bubble departure diameter, bubble inclination angle, upstream contact angle, downstream contact angle and bubble contact diameter were obtained according to the observation. An analysis of force balance on a growing bubble was performed to predict the bubble departure diameter in the narrow channel, and the effect of bubble interface parameters on the prediction of bubble departure diameters was discussed in this paper. The result of predicted model agrees well with the experimental result with a maximum relative deviation less than 25%. According to the study proposed in this paper, the mechanism of bubble departure from a nucleation site can be explained based on the force balance analysis of a growing bubble, and the major forces dominating the bubble departure are the buoyancy force, surface tension force and quasi-steady drag force. 相似文献
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沸腾是一个复杂的换热过程,大量实验表明,不同核化点的脱离直径存在区别,即使在同一工况下,同一核化点产生的汽泡脱离直径也会大小不一,因此汽泡尺寸分布不可忽略。尽管目前已有较多用于汽泡平均尺寸的计算关系式,但对于尺寸分布的研究仍较少。因此,本文针对流动沸腾下汽泡脱离直径的尺寸分布进行研究,对比常用的伽马函数和正态分布函数描述这一分布时的准确度,确定概率函数后,再对概率密度函数中两个重要的参数均值和标准差进行分析,最后得到一套预测不同工况下汽泡尺寸分布的关系式,该关系式准确度较高,并考虑了壁面过热度、质量流速等因素的影响。 相似文献