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Investigation of Two-Phase Liquid-Droplet Flow With Particle Deposition in the Heat Exchanger

机译:热交换器中颗粒沉积两相液滴流的研究

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This article presents a numerical study of particle deposition in two fluids, i.e., liquid and droplet flow in a single row tube bundle heal exchanger. The tubes in the heat exchanger are modeled as heating sources. Two level-set functions are used to capture the liquid-droplet interface and the liquid-deposit front. The effects of different parameters, including Damkohler number, thermal conductivity of the deposit, viscosity of the liquid, and the heating power of the tube on the flow and heat transfer, are investigated. The deposit profiles on the tube surface are analyzed. Comparison is made for the averaged Nusselt number for the case without and with deposition. It is found that the tube surface has a thicker deposit at the upstream facing side compared with that of the downstream facing side. Generally, the heat transfer rate reduces with the growth of the deposit. Under certain conditions, heat transfer can be increased because of the increase in fluid velocity due to blockage of the flow area by the deposit. The averaged Nusselt number oscillated temporally in response to the droplet movement across the tube. Generally, the temperature at the liquid-deposit front decreases with thicker deposit formed. The averaged Nusselt number along the liquid-deposit front increases to a critical value initially, and it starts to decrease with the growth of the deposit.
机译:本文介绍了两个流体中的颗粒沉积的数值研究,即液体和液滴在单个行管束治疗交换器中的液体和液滴流动。热交换器中的管被建模为加热源。两个液位集功能用于捕获液滴接口和液体沉积前部。研究了不同参数,包括达摩人数,沉积物的导热系数,液体粘度的热导率以及管在流动和热传递上的加热功率。分析管表面上的沉积物。对壳体的平均良好编号进行比较,没有沉积。结果发现管表面在上游侧的上游侧具有较厚的沉积物,与下游侧的侧面相比。通常,传热速率随着矿床的生长而降低。在某些条件下,由于沉积物堵塞由于流量面积的堵塞,可以增加热传递。响应于管中的液滴运动,平均衬列数在时间上振荡。通常,液体沉积前部的温度随着形成的厚度较厚的沉积物而降低。沿液体沉积前的平均纽带数最初增加到临界值,并且开始随着沉积物的生长而降低。

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