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首页> 外文期刊>Journal of Fluid Mechanics >THE MOTION OF LONG BUBBLES IN POLYGONAL CAPILLARIES .1. THIN FILMS
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THE MOTION OF LONG BUBBLES IN POLYGONAL CAPILLARIES .1. THIN FILMS

机译:多边形毛细管中的长气泡运动1。薄膜

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摘要

Foam in porous media exhibits an unusually high apparent viscosity, making it useful in many industrial processes. The theology of foam, however, is complex and not well understood. Previous pore-level models of foam are based primarily on studies of bubble flow in circular capillaries. A circular capillary, however, lacks the corners that characterize the geometry of the pores. We study the pressure-velocity relation of bubble flow in polygonal capillaries. A long bubble in a polygonal capillary acts as a leaky piston. The 'piston' is reluctant to move because of a large drag exerted by the capillary sidewalls. The liquid in the capillary therefore bypasses the bubble through the leaky corners at a speed an order higher than that of the bubble. Consequently, the pressure work is dissipated predominantly by the motion of the fluid and not by the motion of the bubble. This is opposite to the conclusion based on bubble flow in circular capillaries. The discovery of this new flow regime reconciles two groups of contradictory foam-flow experiments. Part 1 of this work studies the fluid films deposited on capillary walls in the limit Ca-->0 (Ca = mu U/sigma, where mu is the fluid viscosity, U the bubble velocity, and sigma the surface tension). Part 2 (Wong et al. 1995) uses the film profile at the back end to calculate the drag of the bubble. Since the bubble length is arbitrary, the film profile is determined here as a general function of the dimensionless downstream distance x. For 1 much less than x much less than Ca-1, the film profile is frozen with a thickness of order Ca-2/3 at the centre and order Ca at the sides. For x similar to Ca-1, surface tension rearranges the film at the centre into a parabolic shape while the film at the sides thins to order Ca-4/3. For x much greater than Ca-1, the film is still parabolic, but the height decreases as film fluid leaks through the side constrictions. For x similar to Ca--5/3, the height of the parabola is order Ca-2/3. Finally, for x much greater than Ca--5/3, the height decreases as Ca(1/4)x(-1/4). [References: 26]
机译:多孔介质中的泡沫表现出异常高的表观粘度,使其可用于许多工业过程。然而,泡沫的神学是复杂的并且尚未被很好地理解。以前的泡沫孔隙水平模型主要基于圆形毛细管中气泡流动的研究。然而,圆形的毛细管缺少表征孔的几何形状的角。我们研究了多边形毛细管中气泡流动的压力-速度关系。多边形毛细管中的长气泡充当泄漏的活塞。由于毛细管侧壁施加了很大的阻力,“活塞”不愿移动。因此,毛细管中的液体以比气泡高一个数量级的速度绕过气泡通过泄漏角。因此,压力功主要通过流体的运动而不是气泡的运动来消散。这与基于圆形毛细管中气泡流动的结论相反。这种新的流动方式的发现调和了两组矛盾的泡沫流动实验。这项工作的第1部分研究了在极限Ca-> 0(Ca = mu U / sigma,其中mu是流体粘度,U是气泡速度,sigma是表面张力)下沉积在毛细管壁上的流体膜。第2部分(Wong等,1995)使用后端的胶片轮廓来计算气泡的阻力。由于气泡长度是任意的,因此在此将薄膜轮廓确定为无量纲下游距离x的一般函数。对于远小于Ca-1的x远小于Ca-1的x,薄膜轮廓被冻结,其中心厚度为Ca-2 / 3,而侧面厚度为Ca。对于类似于Ca-1的x,表面张力将薄膜的中心重新排列成抛物线形状,而侧面的薄膜变薄以使Ca-4 / 3排列。对于比Ca-1大得多的x,薄膜仍是抛物线形的,但高度会随着薄膜流体从侧面收缩处泄漏而降低。对于类似于Ca--5 / 3的x,抛物线的高度约为Ca-2 / 3。最后,对于远大于Ca--5 / 3的x,高度随Ca(1/4)x(-1/4)减小。 [参考:26]

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