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| 1 | T型微小通道内两相流分流与分离调控研究进展显示文摘T型通道内的两相流流动和传递过程广泛存在于石油化工、生物制药、电子冷却等领域,而伴随社会进一步微型化、精细化的需求,微小尺度下T型通道内的流动过程及界面受力分析研究的重要性逐渐凸显。尺度的减小使得流动过程中主导作用力由重力等体积力转变为毛细力等表面力,界面运动及相作用机理也随之发生变化;同时,在微尺度下,等径与非等径T型微通道使得两相流流动呈现相分流和相分离两种具有本质区别的流动规律。从小尺度、微尺度和跨尺度三个方面对T型微小通道内两相流分流与分离的研究进展进行整理和分析。目前,等径微通道中相分流的研究多以实验为主,探索各种因素对两相分流特性的影响,诸如入口流型、表观速度、表面张力等;而真正针对非等径微通道内实现相分离的研究较少,且仅限于关注实现两相完全分离的条件及分离性能。鉴于微尺度尤其是非等径跨尺度T型微通道内相分离界面运动复杂、界面受力难于测量等原因,直至如今,相分离过程中的界面受力分析、分离机理以及相分布的主动调控仍是阻挡多孔结构在多相工质中高效利用的关键科学问题;急需实验与数值相耦合的机理研究,最终实现简单多孔结构在实际多相流场合中的广泛应用。 | 陈宏霞 宫逸飞 丁兴起 | 2019 | 科学技术与工程2019，19，31： | 5 |
| 2 | Condensation heat transfer enhancement mechanism for vertical upflows by the phase separation concept at small gravity显示文摘In the field of aerospace, minimum and seal of equipments cause the increase in the thermal loading sharply. Due to the lack of driving force, the performance of conventional condenser deteriorates greatly under the small gravity environment, which leads to reduction in the service life of equipments. In this study, a passive condenser, developed on basis of the phase separation concept,is utilized to improve the performance of the condensation heat transfer under the small gravity environment. As a result of the limitation of experiments, the mechanisms of heat transfer enhancement of the phase separation condenser tube are revealed through numerical simulation based on the volume-of-fluid(VOF) method. The following conclusions could be obtained:(1) A novel phase distribution of ‘‘gas near the tube wall and liquid in the tube core'' is formed. The thin liquid film is indeed created after the flow pattern modulation by inserting mesh cylinder.(2)The condensation quantity for single bubble in the annular region increases about 16 times greater than that in the bare tube region in the case of Jl= 0.0574 m/s and Jg= 0.0229 m/s.(3) Gas volume fraction affects the parameters of liquid film thickness, bubble length and liquid bridge length. The increase in the gas volume fraction results in the decrease in the evaluation index from21.56 to 12.82. The evaluation index is defined as the ratio of the condensation quantities per unit tube length of the annular region and the bare tube region. | Qicheng Chen Dongliang Sun | 2015 | Science Bulletin2015，60，20： | 2 |
| 3 | Significant heat transfer enhancement for R123 condensation by micromembrane cylinder显示文摘Renewable energy or low grade energy utilizations need high performance of phase change heat exchangers. Suspending micromembrane cylinder in tube(called modulated heat transfer tube) increases the void fractions or vapor qualities near the tube wall to significantly enhance heat transfer. The R123 condensation heat transfer with horizontal position was investigated. The results for the bare tube and modulated heat transfer tube were tested case by case. It is found that the modulated heat transfer tube significantly enhance the condensation heat transfer, with the heat transfer enhancement factors(EF)covering the range of 1.118–2.124. The comprehensive performance evaluation criteria(PEC) had the range of0.71–1.66, with most of runs behaving PEC larger than 1.0.For the two-phase outlet conditions, the EF values are increased with increases in the vapor mass fluxes, Gxin,where G is the mass flux and xinis the inlet vapor mass quality. The EF values are inversely related to Gxinfor the subcooled liquid outlet cases. The enhanced heat transfer mechanisms are analyzed with the observed images together with the discussion of pressure and velocity distributions. | Jian Xie Feng Xing Jinliang Xu Huan Liu | 2014 | Chinese Science Bulletin2014，59，28： | 1 |
| 4 | 主动气液调配换热器的研究现状显示文摘在气液相变过程中实施气液调配来主动调节干度和流量,可实现同时提升传热系数(h)和降低压降(Δp)。本文从气液调配强化传热原理、气液调配单元和气液调配换热器三个方面,总结国内外研究现状。主动气液调配在冷凝过程(分液冷凝)和蒸发过程(配液蒸发)中均需使工质处于高效传热区,但目标干度不同。重点关注了有联箱-小孔型、T型管和金属丝网这三类气液调配单元,发现低质量流量下联箱-小孔型与T型管的分液比率(F L)可达100%,而金属丝网型仅为30%。分液冷凝器的表面传热系数相比常规换热器可提升112%,但蒸发过程的气液调配研究较少,调配机理尚不清晰,需要进一步开展研究。气液调配式换热器的性能与气液分离效率(η)和支管的干度与流量分配紧密相关,基于多维联合仿真法综合考虑气液两相在联箱内的流态(气泡、液膜和液滴)、气液相界面传质和管道压降等影响因素有望提升气液调配换热器模型的预测精度。 | 黄锟腾 陈健勇 陈颖 罗向龙 梁颖宗 何嘉诚 施永康 | 2023 | 制冷学报2023，44，3： | 0 |
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