球形液膜动态特性的研究

对球形液膜内气体沿细管排出过程中，球形液膜的动态特性进行了模拟和验证。     

气体粘滞系数的测定

本文对球形液膜内气体沿细管排出过程中，球形液膜的动态特性作了理论模拟推导，并用该实验装置对常温下空气的粘滞系数进行了测定。     

液体表面现象的演示设计

介绍了有关液体表面层、单液膜和双面膜球形气泡内外压强差的比较以及毛细现象中液面高度随半径变化规律的演示设计和实验方法.     

气体激光管的球形镀铝阴极

1)本发明专利号8710344.3. 本发明涉及气体激光管的阴极,为气体激光管提供了一种球形整体结构镀铝阴极.阴极壳与激光管用同一种玻璃质材料制成一体.在阴极壳内表面镀上一层铝膜作为阴极,该铝膜覆盖整个球形内表面.伸入该球形整体结构阴极内部的激光管的放电毛细管,与该球形阴极壳的一个开口的伸入部分相交错并连通,该伸入部分的端口位于该球形整体结构阴极的球心附近,能使该球形阴极表面各处的放电电流密度相对于该放电管开口是均匀分布的,从而减少了阴极溅射,保证气体的重新释放与气体的俘获达到平衡,降低了“气体清除”效应,延长了气体激…     

波纹管内R113降膜流动特性的结构影响研究

为设计适用于有机工质余热发电降膜蒸发装置,采用FLUENT VOF法建立了气-液两相逆流流动CFD模型,对氟利昂(R113)波纹管内气液两相逆流降膜进行数值模拟,研究了管长、波峰、波间距对波纹管内降膜流动的影响。研究结果表明:在一定喷淋密度下,液膜稳定性随波纹管长的增大而降低,液膜的波动性随波纹管长的增大而增强,当管长小于某个值时,液膜沿壁面均匀分布,存在最佳管长;波间距越大,液膜波动越强,增加波间距能够增加液膜稳定性;波峰越大,液膜沿管长方向的变化越剧烈,减小波动幅度可以增加液膜均匀性。     

液滴碰撞对液膜内汽泡运动与换热影响

采用数值模拟的方法,研究了沸腾雾化喷射过程中热壁面薄液膜层受到液滴碰撞扰动时液膜层内汽泡运动,相界面变化和由此引起的壁面换热特性.模拟结果显示汽泡生长初期相界面变化与液膜层内二次核化特征与文献结果吻合良好,汽泡生长后期相界面变化存在滞后.讨论了液滴下降速度.液滴直径与初始位置,多液滴碰撞对液膜层内流动与壁面换热的影响.     

PAMS微球制备过程中电解质的影响

为调控固化过程中双重乳液内径的变化和降低聚-α-甲基苯乙烯(PAMS)微球的表面粗糙度,研究了双重乳液固化过程中内外水相中电解质浓度对水在油相液膜中迁移和分相行为的影响。结果表明:仅在外水相中添加电解质时,内水相的渗透压高于外水相,使得内相水向外水相迁移,导致固化后的微球表面起皱。当在内外水相同时添加电解质时,由于平衡了三相之间水的化学势,抑制了水在油相液膜中的迁移和分相,导致PAMS微球壳壁内气泡体积和数量显著降低。同时,在内外水相中同时添加不同浓度的电解质,还可显著改善双重乳液三相之间的密度匹配度,从而提高微球的球形度和壁厚均匀性。     

液膜气泡法测洗涤溶液的表面张力系数

利用自制装置采用液膜气泡法测定了洗涤溶液的表面张力系数．由医用注射器充气形成球形液泡，通过与之连通的微压计测出液泡内外的压强差，运用杨氏-普拉斯方程计算出洗涤溶液的表面张力系数.     

可压缩气体中带电Newton流体平面液膜的不稳定性分析

液体雾化被广泛应用于工业、农业等领域,雾化过程中液体首先形成液膜,液膜在气液边界层内出现不稳定,导致液膜破碎。因此液膜的不稳定性对液体雾化起着非常重要的作用,有必要对液膜的不稳定性进行研究。采用数值计算的方法对可压缩气体中黏性平面液膜的不稳定性进行了研究,首先对黏性平面液膜和气体的速度分布进行推导,在此基础上采用谱方法对黏性平面液膜的不稳定性进行了研究。研究发现：在正弦和曲张模式下,施加电场会加速平面液膜的破碎;正弦模式比曲张模式更加不稳定,说明正弦模式在平面液膜不稳定中起主导作用;气体Mach数、电Euler数、气体Reynolds数、 Weber数和动量通量比的增加会加速液膜的破裂;随着气体边界层与液膜厚度比和液体Reynolds数的增加,扰动波的增长速率降低,液膜变得更加稳定。     

离心式喷嘴内气液两相流动的数值模拟

求解三维不可压NS方程,并应用VOF方法捕获气液分界面,计算不同压降下离心式喷嘴内的气液两相流动状况,研究了不同压降对喷嘴内流动的影响。计算很好地模拟了喷嘴内的气液两相流动,并得到了出口液膜速度、喷雾锥角以及液膜厚度等参数,数值计算所得结果同试验符合得较好,好于经验公式的结果。     

模拟合成孔径雷达数据片波差的测量和胶片、波差的容限

本文介绍一种用马赫-陈德干涉系统测量模拟合成孔径雷达数据片波差的方法.该法能把两种原因产生的波差区分开来,即把通过胶片变形的波面与平面参考波面比较,求出胶片厚度不平产生的波差;把合成孔径雷达数据片的一级衍射波面与两个半径不等的参考球面波比较,分别求出由模拟装置产生的方位维和斜距维波差.本文给出一些实验结果和分析.这种方法还可以用于测量真实合成孔径雷达数据片的波差.由胶片厚度变化产生的波差可以用液体门补偿.但是,在实际中使用液体门是很繁复的,有时也没有必要.因此,我们认瑞利准则出发导出合成孔径雷达数据片胶片厚度变化产生的波差的容限,以此作为判断是否要用液体门的依据.     

单液滴正碰球面动态行为特性实验研究

在考虑空气阻力影响,确定液滴撞击球面速度的基础上,对较高韦伯数液滴撞击干燥球面动态行为过程进行了实验研究,分析了球面曲率与韦伯数对液滴撞击行为和铺展因子的影响,并与前人撞击平面结果进行了对比.实验表明,靠近撞击球面时,液滴降落速度出现明显波动;球面曲率对液滴撞击后行为影响明显,曲率较大时,液滴撞击后铺展液膜会超出球面直径并滑落,曲率较小时,液滴撞击后在球面上呈现明显的铺展、回缩、震荡、着附动态变化行为,此时最大铺展因子受曲率影响小,随曲率减小,逐渐趋向于撞击平面时的最大铺展因子;韦伯数对液膜铺展速率影响较小,但对液膜回缩时间影响明显,最大铺展因子随韦伯数增加逐渐增大,获得的关联式呈指数变化.     

Critical assessment of effective interfacial potentials based on a density functional theory for wetting phenomena on curved substrates

In this Letter we examine an effective interfacial Hamiltonian approach for wetting phenomena based on two different density approximations in the framework of a density functional theory. The system under consideration is an attractive spherical wall subject to adsorption by a metastable liquid. We argue that, contrary to a planar geometry, in the spherical case the popular sharp-kink approximation leads to a considerable disagreement for the film thickness with numerical results obtained from density functional theory. We show that the deviation originates from the inaccuracy of the predicted liquid-gas surface tension. We further demonstrate that the prediction can be substantially improved when a soft-interface approximation is adopted, such that the liquid-gas interface is approximated by a smooth monotonic function.     

冷凝器壁面滴状冷凝的热力学机理及最佳接触角

应用自由能判据证明了冷凝器壁面液滴的力学平衡条件与接触角有关,进而证明了当壁面液滴与壁面的接触大于90°时,冷凝器壁面液滴的化学势将小于同曲率的球形液滴的化学势;另外,在相同饱和比下,壁面液滴的临界半径也小于球形液滴的临界半径.而在接触角小于90°时,情况则恰好相反.正是由于这双重原因,使得滴状冷凝的传热性能大大优于膜状冷凝的传热性能,并由此求出了冷凝器壁面液滴的最佳接触角. 关键词：     

Forced convection heat transfer around large two-phase bubbles condensing in an immiscible liquid

In this investigation, an equation is theoretically developed to predict the Nusselt number and hence the collapse rate of large spherical two-phase bubbles condensing in quiescent immiscible liquid. Heat transfer from the thin film of condensate and in the wake is determined. Theoretical prediction and experimental data show satisfactory agreement. A parametric study is also carried out for different parameters affecting the collapse rate.     

存在液膜的毛细蒸发过程研究

采用水浴恒温蒸发方法研究了液膜存在时的毛细蒸发过程. 研究结果表明：毛细蒸发过程中液/气界面符合黏性指延,且不受蒸发速度及液膜状态的影响;蒸发过程可分为剧烈减速、匀速蒸发、线性减速蒸发和边界效应四个阶段,分别对应不同的液膜状态;毛细蒸发的主要区域在毛细管端口液膜处,工质由液体区流向端口蒸发区的过程中液膜起到了通道桥梁作用. 关键词： 毛细蒸发 液/气界面 蒸发阶段 液膜     

Effect of the initial phase state of DT-matter on the compression of inertial fusion targets

We investigate the efficiency of inertial fusion target compression, where at the initial time moment the thermonuclear fuel is in a two-phase state and has the form of two adjacent layers — the external DT-liquid layer and the internal DT-ice layer. We study this problem for the fast ignition targets, where the ultimate final density of the thermonuclear matter is of a special importance. We take the simplest type of a fast ignition target, which corresponds to the technical justification of the HiPER Project aimed at demonstrating fast ignition at the compressing laser pulse energy ~100 kJ. Such a target presents a spherical DT-ice shell coated with a thin polymer film. We obtain the dependence of the final target density on the mass fraction of the DT-matter liquid phase and formulate the requirements on the admissible concentration of liquid phase if the decrease in the DT-fuel final density does not exceed 10%. We find the criterion for choosing the laser-pulse duration which provides the minimum decrease in the final density of the target containing DT-matter in the initial two-phase state.     

Numerical Simulation for Falling Film Flow Characteristics of Refrigerant on the Smooth and Structured Surfaces

Flow characteristics of a liquid film flowing over a smooth surface and structured surface with the Reynolds number range from 10 to 1121 are studied. The mixture of R21 and R114 refrigerants is used as the test liquid. The 3D transient simulations are taken to capture the liquid film’s dynamic characteristics and spatial distribution. Effects of the inlet dimension, inlet flow rates, surface tension, and surface structuring on the wettability, average velocity, and film thickness are studied systematically. The obtained results show that surface tension is essential for an accurate simulation, while inlet width has no effect on the liquid film parameters in the steady-state flow regime. For low flow rates, wetting area and film thickness both are small, and a suggested range of Reynolds number is chosen to simulate further heat transfer in order to balance the film thickness and dry spots generation. It is shown that a ripple surface structure hinders the liquid film movement, reflected in a lower velocity and a larger film thickness compared to the smooth surface. Lateral movement of a liquid film can also be observed at the structured surface.