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燃煤烟气中的含细微颗粒物浆滴经烟气夹带进入大气会对电厂周边环境造成较大的危害.高效脱除含细微颗粒物的湿烟气冷凝液滴是防控细微颗粒物污染的有效手段,而细微颗粒物在液滴内部的流动与沉降行为对液滴脱除滑动特性有重要影响.基于此,本文建立了微米尺度固体颗粒在二维单液滴内的自由沉降运动模型,数值模拟研究了颗粒粒径、液滴形貌参数、... 相似文献
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《工程热物理学报》2017,(2)
通过推导液滴在蒸发过程中,边界是否考虑Marangoni应力作用时,其内部流场分布的极坐标解析式,并结合相应的球冠液滴模型,来描述液滴内部的流线分布情况,以及液滴在受到Marangoni应力作用时,极坐标下ρcosα=常数处速度随液滴高度的分布规律。并分别使用实验与数值模拟结果与解析结果进行对比,从而说明解析式的正确性。同时从液滴的流线的分布得出:液滴在蒸发过程中,其内部的流动速率在三相界面处最大,在靠近基板的中心处最小。受Marangoni应力作用的影响,液滴内部在其对称面上产生了环流,其方向在液滴底部是从液滴中心流向三相界面的,同时也说明了Marangoni对流可以抑制"咖啡环"效应。 相似文献
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液滴在固体表面上的铺展行为与润湿特性对许多工业生产过程的研究具有重要意义.根据液滴在光滑表面上的受力情况,建立了液滴平壁铺展的动力学模型.应用润滑近似方法和二维Navier-Stokes方程,建立了液滴沿理想表面铺展的动量和连续性方程.根据建立的方程,应用数值解法求解并详细分析了液滴在铺展过程中膜厚、接触线铺展半径以及铺展速度随时间的变化关系.研究结果表明:液滴的铺展过程可分为扩展和收缩两个阶段,铺展过程伴随着表面能、动能以及各种势能的相互转化,液滴最终的铺展半径大小由固体基面固有的润湿特性所决定;液滴在铺展过程中出现的"坍塌效应"与弯曲液面处的Laplace压力差有关;铺展半径随时间变化的标定律近似满足"1/7"次方标度律. 相似文献
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发展建立了用于多体分离等包含动边界的非定常流场数值模拟方法,建立了笛卡尔坐标系下边界以任意速度运动的控制体上的流动控制方程,结合几何守恒律确定网格速度,发展了基于结构网格的动网格方法,网格移动量采用加权插值方法得到.通过数值模拟二维翼型及三维机翼的强迫振荡非定常流场,表明该方法可以数值模拟包含动边界的非定常流场. 相似文献
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Results of a parametric study of pressure characteristics of a perforated membrane in an oscillating liquid flow are reported. A diagram of an experimental facility for evaluation of the pressure produced by a perforated membrane in an oscillating flow is given. 相似文献
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本文以水蒸汽为工质对水平三维微肋管内凝结换热及阻力特性进行了实验研究.与光管和二维管相比,在相同条件下,实验中效果最好的T3管全长平均凝结换热系数分别提高了113%~410%和20%~65%,同时,与二维管相比流动阻力增加较小,最大值不超过6.3%.比较另两种管型(T1,T2管)也证明三维管以较小的流阻增加为代价换取了明显的强化效果. 相似文献
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水平内微肋管局部凝结换热性能实验与数值求解 总被引:1,自引:0,他引:1
以R11为工质,蒸汽凝结压力为147-265kPa,质量流率4ty153kg/m2s,本文对二维内微肋管和三维内微肋管水平管内凝结分层流区局部换热系数进行了系统的实验。与光管比较,二维内微肋管和三维内微肋管局部凝结换热系数分别提高了147-783%和261-997%。本文首次从理论分析入手建立了二维内微肋管水平管内凝结分层流区局部换热系数分析模型并进行了数值求解。计算结果与本文实验相当吻合。 相似文献
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Results of a study of the flow rate — pressure head characteristics of a perforated membrane immersed in an oscillating liquid flow are reported; such characteristics need to be known when hydropneumodiodes are used as a pump. We show that the perforation pattern (or, more specifically, the number of perforated holes) affects just the rate of the liquid flow through membrane. 相似文献
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Results are reported on a combined experimental and numerical investigation of a free surface flow at small Reynolds numbers. The flow is driven by the rotation of the inner of two horizontal concentric cylinders, with an inner to outer radius ratio of 0.43. The outer cylinder is stationary. The annular gap is partially filled, from 0.5 to 0.95 full, with a viscous liquid leaving a free surface. When the fraction of the annular volume filled by liquid is 0.5, a thin liquid film covers the rotating inner cylinder and reenters the liquid pool. For relatively low rotation speeds, the evolution of the film thickness is consistent with the theory for a plate being withdrawn from an infinite liquid pool. The overall liquid flow pattern at this condition consists of two counter-rotating cells: one is around the inner cylinder and the other with weaker circulation rate is in the bottom part of the annulus and nearly symmetric about the vertical axis. With increasing rotation rate, the free surface becomes more deformed, and the dynamics of the stagnation line and the cusp line dividing the cells are tracked as quantitative measures of the interface shape. In addition, the recirculating flow cells lose symmetry and the cusp deforms the free surface severely. A comparison of numerically computed flow which describes the interface by a phase-field method confirms the dynamics of the two cells and the interface deformation. For filling fraction 0.75, the liquid level is slightly above the inner cylinder and a significant decrease in size of the bottom cell with increasing rotation rate is found. For filling fractions approaching unity, the liquid flow consists of one single cell and the surface deformation remains small. 相似文献