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Experimental study on flow patterns for water boiling in horizontal heated tubes

机译:水平加热管中水沸腾流动方式的实验研究

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摘要

An experimental study on flow patterns for water boiling in horizontal heated tubes was conducted to observe the evolution and transition of flow patterns while controlling various parameters, such as heat flux, mass velocity, and tube diameter. Six boiling flow patterns are observed in the test tubes, namely, bubble, plug, slug, wave, stratified, and annular flows, which can be further classified into three types based on their various characteristics: intermittent, stratified-wave, and annular flows. The evolution of flow patterns for water boiling in horizontal heated tubes was significantly affected by heat flux, mass velocity, and tube diameter. The increment of heat flux pushed the starting point of each flow pattern toward the inlet of the tube. Intermittent and stratified-wave flows occurred at lower mass velocity, and annular flow occurred with an increase in mass velocity. Moreover, annular flow easily appeared in tubes with smaller diameters. Since the heat per unit of mass for the full tube length increases with either an increase in heat flux or a decrease in mass velocity and tube diameter, the transition always occurs at smaller vapor qualities with the increase of the heat per unit of mass during the transition of the three flow patterns. The experimental data in this study were compared with the adiabatic flow pattern maps proposed by Baker, Mandhane, Taitel, and Weisman. Based on the experimental data, a new flow pattern map for water boiling was proposed for predicting flow patterns in horizontal heated tubes.
机译:对水平加热管中水沸腾的流型进行了实验研究,以观察流型的演变和转变,同时控制各种参数,例如热通量,质量速度和管直径。在试管中观察到六种沸腾流型,即气泡,塞子,段塞,波动,分层和环形流,根据它们的各种特性可将其进一步分为三种类型:间歇流,分层波和环形流。水平加热管中水沸腾的流型演变受热通量,质量速度和管径的显着影响。热通量的增加将每个流型的起点推向管子的入口。间歇波和分层波流以较低的质量速度发生,而环形流以质量速度增加发生。而且,在较小直径的管中容易出现环形流动。由于整个管子长度的每单位质量的热量随热通量的增加或质量速度和管径的减小而增加,因此在汽化过程中,随着质量每单位质量的热量的增加,转变总是在较小的蒸汽质量下发生。三种流动模式的过渡。将本研究中的实验数据与贝克,曼丹,泰特尔和魏斯曼提出的绝热流型图进行了比较。基于实验数据,提出了一种新的水沸腾流态图,用于预测水平加热管中的流态。

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