共查询到18条相似文献,搜索用时 171 毫秒
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采用基于Shan-Chen伪势模型的格子Boltzmann方法,对液滴在存在润湿梯度的倾斜表面上克服重力、自下而上运动的过程进行模拟。探究润湿梯度、液滴尺寸、Bond数以及表面倾斜角度对液滴运动的影响。计算结果表明:液滴在运动过程中,内部会出现沿斜面向上的速度矢量,润湿梯度越大,液滴运动速度越快,润湿长度也越长,且动态接触角减小速率越快。液滴尺寸和Bond数对液滴运动的影响较小,但存在临界Bond数,超过该临界Bond数时,液滴将沿梯度润湿表面向下运动。表面倾角对液滴运动有显著影响,倾角增大,液滴运动速度和润湿长度都明显减小。 相似文献
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本文采用高速摄像仪对水滴和乙醇液滴撞击加热壁面后的蒸发过程进行了实验观测, 分析了液滴撞击加热壁面后的蒸发特性参数. 实验中, 两种液体初始温度均为20 ℃, 不锈钢壁面初始温度范围为68-126℃. 水滴初始直径为2.07 mm, 撞击壁面时Weber 数为2-44; 乙醇液滴初始直径为1.64 mm, Weber数为3-88. 结果表明, 液滴受到重力、表面张力及流动性的影响, 在蒸发过程的大部分时间内, 水滴高度持续降低而接触直径几乎不变; 蒸发后期, 液滴发生回缩, 水滴的接触直径、高度和接触角出现振荡现象. 乙醇液滴的接触角随时间的增加呈现先减小随后保持不变的趋势, 而接触直径和高度则持续减小, 直到液滴完全蒸发. 液滴蒸发总时长与液体物性和壁面温度有关, 随壁面温度的升高而减小, 与液滴撞击壁面时的Weber 数无关. 同时, 随着壁面温度的升高, 液滴显热部分占总换热量的比重增大, 显热部分能量不可忽略, 本文实验条件下得到水滴的平均热流密度为0.014-0.110 W·mm-2. 相似文献
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为准确描述汽轮机级内湿蒸汽凝结流动特性,采用双流体模型结合修正的均质成核和水滴生长模型,实现汽轮机初始成核级叶栅通道内非平衡凝结数值求解。通过焓损失系数与自由能理论进一步分析了进汽参数变化对汽轮机叶栅通道内湿蒸汽自发凝结流动的影响,结果表明:随着过热度的降低,非平衡凝结起始位置提前,非平衡凝结现象更剧烈,凝结产生的液相质量分数增加,热力学损失升高;进口湿度对水滴的生长和蒸发速率非常敏感,对凝结冲击位置有很大的影响;入口湿蒸汽液滴直径越大,阻碍相变的自由能壁垒越低,二次凝结现象越易发生,热力学损失越大,当湿度为0.01的液滴直径超过0.2μm时,均质成核的二次凝结现象逐渐发生;二次成核的临界水滴直径随着湿度的增加而增大。 相似文献
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针对高温熔渣粒化技术的开发,本文通过可视化实验研究了高炉渣熔融液滴撞击不锈钢壁面的动态行为特性。结果表明:随液滴雷诺数增大,撞击过程液滴形态演变模式依次由铺展-回缩转变为铺展-回缩破碎和铺展-破碎-凝固;增大壁面粗糙度可减弱与壁面换热,抑制液滴铺展;减小壁面粗糙度促进液滴发生破碎;液膜回缩过程普遍出现回卷现象,壁面倾角越大,液膜回卷和液滴滚动现象越显著,且液滴铺展面积越大,在壁面停留时间越长;减小液滴雷诺数、减小壁面粗糙度并采用垂直粒化仓壁面有利于壁面防黏结。 相似文献
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《Surface Science Reports》2014,69(4):325-365
A sessile drop is an isolated drop which has been deposited on a solid substrate where the wetted area is limited by the three-phase contact line and characterized by contact angle, contact radius and drop height. Although, wetting has been studied using contact angles of drops on solids for more than 200 years, the question remains unanswered: Is wetting of a rough and chemically heterogeneous surface controlled by the interactions within the solid/liquid contact area beneath the droplet or only at the three-phase contact line? After the publications of Pease in 1945, Extrand in 1997, 2003 and Gao and McCarthy in 2007 and 2009, it was proposed that advancing, receding contact angles, and contact angle hysteresis of rough and chemically heterogeneous surfaces are determined by interactions of the liquid and the solid at the three-phase contact line alone and the interfacial area within the contact perimeter is irrelevant. As a consequence of this statement, the well-known Wenzel (1934) and Cassie (1945) equations which were derived using the contact area approach are proposed to be invalid and should be abandoned. A hot debate started in the field of surface science after 2007, between the three-phase contact line and interfacial contact area approach defenders. This paper presents a review of the published articles on contact angles and summarizes the views of the both sides. After presenting a brief history of the contact angles and their measurement methods, we discussed the basic contact angle theory and applications of contact angles on the characterization of flat, rough and micropatterned superhydrophobic surfaces. The weak and strong sides of both three-phase contact line and contact area approaches were discussed in detail and some practical conclusions were drawn. 相似文献
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We study the forced aspiration of small ( mm) and large ( cm) liquid drops, deposited on prewetted porous membranes, and pumped mechanically with a constant current J. Two kinds of membranes are used where the pores are i) disconnected, cylindrical and calibrated or ii) interconnected “sponge-like”.
Whatever the size of the drops and the intensity J of the current, two suction regimes are observed versus time: 1) a “locked” regime, when the drop is pinned, with a dynamic contact angle decreasing from advancing () to finite receding () contact angle; 2) an “unlocked” regime, where the contour line recedes with a constant contact angle closed to . In both regimes, the shape of the drop remains quasistatic, during the suction process, i.e. a spherical cap for small drops and a flat “gravity pancake” for large ones.
Received 19 January 2000 相似文献
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蒸气凝结相关问题探讨 总被引:3,自引:1,他引:2
讨论了几个与蒸气凝结相关的问题,指出壁面上球冠形液滴的内外压差和临界半径同样遵循经典的Laplace公式和Kalvin公式;蒸气在冷壁上的冷凝形态主要由后退接触角决定;空气中的水蒸气在换热器表面呈膜状冷凝时换热器的性能优于呈滴状冷凝时换热器的性能。 相似文献
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X. Jia J. B. McLaughlin K. Kontomaris 《The European physical journal. Special topics》2009,171(1):105-112
Video images of drops colliding with solid surfaces shown by Rioboo et al. (2002) reveal that, for large drop velocities,
the drops flatten and form a ring structure before receding and, in some cases, rebounding from the surface. They described
the sequence of events in terms of four distinct regimes. During the initial kinematic phase, the dimensionless wetting radius
of the drop follows a universal form if the drop Weber and Reynolds numbers are sufficiently large. In the second phase, the
drop becomes highly flattened and the values of the Weber and Reynolds numbers influence the time evolution of the dimensionless
wetting radius and its maximum value. This is followed by a third phase in which the wetting radius begins to decrease with
time and the wettability of the surface influences the dynamics. This paper presents simulation results for the early stages
of drop impact and spreading on a partially wetting solid surface. The simulations were performed with a modified version
of the lattice Boltzmann method (LBM) developed by Inamuro et al. (2004) for a liquid-gas density ratio of 1000. The Inamuro
et al. version of the LBM was modified by incorporating rigid, no-slip boundary conditions and incorporating a boundary condition
on the normal derivative of the order parameter to impose the desired equilibrium contact angle. 相似文献
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Joel L. Plawsky Sashidhar S. Panchamgam Shripad J. Gokhale Peter C. Wayner Jr. Sunando DasGupta 《Superlattices and Microstructures》2004,35(3-6):559
A vertical constrained vapor bubble, VCVB, made of fused silica was used to study the stability and oscillations of an evaporating wetting film of HFE- 7000® in a corner. The film thickness profile was measured as a function of time and axial position using an advanced form of image analyzing interferometry. The curvature, apparent contact angle, and pressure profiles for the evaporating film were calculated from the measured film thickness profiles. Oscillation of the liquid film was observed and profiles for both the advancing and receding films were obtained. These are the first such detailed profiles obtained for an oscillating meniscus below a thickness of 0.1 μm.The film thickness profiles demonstrated the spreading of the meniscus during advance as well as the presence of a curvature gradient near the contact line region. The maximum curvature decreased for the advancing menisci and increased with time for the receding menisci. An increase in the adsorbed film thickness was associated with the advancing stage and a decrease with the receding stage. Pressure profiles were measured as a function of position indicating the potential for driving the flow of the fluid toward or away from the contact line. As the film advances or recedes, the pressure gradients change as a function of position fueling the next oscillation cycle. 相似文献
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