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A mechanistic model for expansion loss coefficient in upward vertical annular flow

机译:垂直向上环形流中膨胀损失系数的力学模型

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Gas-liquid annular flow draws different responses from its three constituents, namely, the liquid film, the entrained liquid droplets and the gas core, as they flow through a diverging section in a pipe. The resulting change in the pressure profile is a combination of several effects associated with the dynamic interactions among these three fields. Accurate simulation of the response using Eulerian-Eulerian computational fluid dynamics is not feasible because the processes are inherently complex and a framework of relevant and validated constitutive relations describing the physical processes is not yet available. In the present work, a simpler approach is adopted by studying the interactions individually in idealized settings, and bringing together the separate effects into a phenomenological model for pressure loss in upward vertical annular flow. The overall pressure change is expressed as a sum of three contributors: change in area of cross-section available for gas flow, change in the effective interfacial roughness leading to peaking of the velocity profile, and droplet-gas momentum exchange in the immediate downstream of the expansion. Using air-water experimental data from two expansion ratios and three half-angles of the diverging sections, a mechanistic correlation is proposed to evaluate the overall pressure loss coefficient. (C) 2018 Elsevier Inc. All rights reserved.
机译:气液环形流在流经管道中的发散段时,会从其三个成分(即液膜,夹带的液滴和气芯)中获得不同的响应。压力分布的最终变化是与这三个场之间的动态相互作用相关联的几种影响的组合。使用欧拉-欧拉计算流体动力学对响应进行准确的模拟是不可行的,因为这些过程本质上是复杂的,并且尚无描述物理过程的相关且经过验证的本构关系框架。在当前的工作中,采用一种更简单的方法,即在理想的环境中单独研究相互作用,并将单独的影响集中到现象学模型中,以进行向上垂直环形流动的压力损失。总体压力变化表示为三个因素的总和:可用于气体流动的横截面面积的变化,导致速度曲线达到峰值的有效界面粗糙度的变化以及在紧邻下游的液滴气体动量交换扩展。利用分叉截面的两个膨胀比和三个半角的空气-水实验数据,提出了一种力学相关性来评估总的压力损失系数。 (C)2018 Elsevier Inc.保留所有权利。

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