微通道流动沸腾中表面润湿性对气泡动力学和传热的影响

IF 5.8 2区 工程技术 Q1 ENGINEERING, MECHANICAL International Journal of Heat and Mass Transfer Pub Date : 2025-05-15 Epub Date: 2025-01-23 DOI:10.1016/j.ijheatmasstransfer.2025.126729
Yanhong Sun , Zan Zhang , Guotao Zhang , Yuyan Jiang , Jun Zheng
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引用次数: 0

摘要

尽管对宏观沸腾过程中气泡动力学控制进行了广泛的研究和建模,但表面润湿性对微通道沸腾过程中气泡动力学的影响却很少被研究。微通道的限制和主导力的波动导致了独特的受限气泡生长和独特的气泡分离。表面润湿性会显著影响气泡动力学参数,从而影响微通道流动沸腾的传热性能。在本研究中,我们以HFE-7100为工作流体,通过过冷流动沸腾实验和流动可视化,定量研究了表面润湿性对微通道中滑动气泡动力学、受限气泡生长和传热特性的影响。由于疏水表面气泡成核的能垒较低,许多成核位点被激活。拉长后的气泡形状更平坦,气泡尺寸更大,这可能是由于疏水表面的气泡附着力较强。气泡在亲水性表面上的滑动和生长速度要高得多,气泡加速度增加了气泡周围的剪应力和压力梯度,使气泡呈非轴对称斜三角形轮廓。亲水表面的气泡生长速率大约是疏水表面的3倍。在质量通量为112 kg·m−2·s−1和230 kg·m−2·s−1的微通道沸腾过程中,由于大量气泡成核位点的活化,疏水表面的传热系数分别提高了82%和25%。此外,由于微对流的加强和环空流动的抑制,高质量通量下的热通量增加了56%。微通道沸腾传热以核状沸腾机制为主。
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Effect of surface wettability on bubble dynamics and heat transfer in microchannel flow boiling
Despite extensive studies and modeling of bubble dynamics manipulation in macroscale boiling, the effect of surface wettability on the bubble dynamics of microchannel flow boiling has seldom been investigated. The confinement of the microchannel and fluctuations in the dominant forces lead to unique confined bubble growth and distinctive bubble detachment. Surface wettability can significantly affect the bubble dynamics parameters, thereby influencing the heat transfer performance of microchannel flow boiling. In this study, we conducted subcooled flow boiling experiments and flow visualizations to quantitatively investigate the influence of surface wettability on sliding bubble dynamics, confined bubble growth, and heat transfer characteristics in a microchannel using HFE-7100 as the working fluid. Numerous nucleation sites were activated owing to the lower energy barrier for bubble nucleation on the hydrophobic surface. The elongated bubble shape was flatter, and the bubble size was larger, which could be attributed to the strong bubble adhesion force on the hydrophobic surface. The bubble sliding and growth velocities were much higher on the hydrophilic surface, and bubble acceleration increased the shear stress and pressure gradient surrounding the bubble, producing a more non-axisymmetric oblique triangle profile of the elongated bubble. The bubble growth rate on the hydrophilic surface was approximately three times higher than that on the hydrophobic surface. The heat transfer coefficients (HTCs) on the hydrophobic surface increased by up to 82 % and 25 % during microchannel flow boiling at mass fluxes of 112 and 230 kg·m−2·s−1, respectively, because of the activation of numerous bubble nucleation sites. Furthermore, the HTCs increased by up to 56 % for higher mass fluxes owing to the strengthening of microconvection and suppression of annular flow. The nucleate boiling mechanism dominated the microchannel flow boiling heat transfer.
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来源期刊
CiteScore
10.30
自引率
13.50%
发文量
1319
审稿时长
41 days
期刊介绍: International Journal of Heat and Mass Transfer is the vehicle for the exchange of basic ideas in heat and mass transfer between research workers and engineers throughout the world. It focuses on both analytical and experimental research, with an emphasis on contributions which increase the basic understanding of transfer processes and their application to engineering problems. Topics include: -New methods of measuring and/or correlating transport-property data -Energy engineering -Environmental applications of heat and/or mass transfer
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