首页> 外文期刊>International Journal of Heat and Mass Transfer >Effects of two-phase inlet quality, mass velocity, flow orientation, and heating perimeter on flow boiling in a rectangular channel: Part 1 - Two-phase flow and heat transfer results
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Effects of two-phase inlet quality, mass velocity, flow orientation, and heating perimeter on flow boiling in a rectangular channel: Part 1 - Two-phase flow and heat transfer results

机译:两相入口质量,质量速度,流向和加热周长对矩形通道中流沸腾的影响:第1部分-两相流和传热结果

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Lack of understanding of flow boiling behavior in reduced gravity poses a major challenge to the development of future space vehicles utilizing two-phase thermal control systems (TCSs). A cost effective method to investigating the influence of reduced gravity on flow boiling is to perform ground experiments at different orientations relative to Earth gravity. This paper is the first part of a two-part study aimed at exploring flow boiling mechanisms of FC-72 in a rectangular channel heated along one wall or two opposite walls. Experiments are performed in vertical upflow, vertical downflow and horizontal flow, subject to large variations in mass velocity, inlet quality and wall heat flux. Detailed measurements are used to investigate the influences of orientation, and therefore gravity, on boiling curve, local and average heat transfer coefficients, and pressure drop, and their relationship with interfacial behavior is captured with high-speed video. For horizontal flow, the effects of gravity are reflected in appreciable stratification across the channel at low mass velocities, with gravity aiding vapor removal from, and liquid return to the bottom heated wall, while accumulating vapor along the top heated wall. For vertical upflow and vertical downflow, with both single-sided and double-sided heating, there is far better symmetry in vapor formation along the channel. The heat transfer coefficient shows significant variations among the different orientations and heating configurations at low mass velocities, but becomes insensitive to orientation above 800 kg/m~2 s, proving inertia around this mass velocity is effective at negating any gravity effects. For low mass velocities, pressure drops are fairly equal for vertical upflow and vertical downflow, but greater than for horizontal flows. However, fairly equal pressure drops are achieved at high mass velocities for all orientations. Overall, this study proves that gravity effects on two-phase pressure drop and two-phase heat transfer are dictated mostly by mass velocity and, to a lesser extent, by inlet quality.
机译:缺乏对降低重力中的沸腾行为的了解,对使用两相热控制系统(TCS)的未来航天器的发展提出了重大挑战。研究降低的重力对流动沸腾的影响的一种经济有效的方法是在相对于地球重力的不同方向上进行地面实验。本文是由两部分组成的研究的第一部分,旨在探讨FC-72在沿一个壁或两个相对壁加热的矩形通道中的沸腾机理。实验在垂直向上,垂直向下和水平流动中进行,但要注意质量速度,入口质量和壁热通量的较大变化。详细的测量用于调查取向以及重力对沸腾曲线,局部和平均传热系数以及压降的影响,并通过高速视频捕获它们与界面行为的关系。对于水平流动,重力的影响以较低的质量速度反映在整个通道的明显分层中,重力有助于从底部加热的壁中除去蒸气,并使液体返回底部加热的壁,同时沿顶部加热的壁积聚蒸气。对于垂直加热和垂直下降,同时采用单面和双面加热,沿通道形成蒸汽的对称性要好得多。在较低的质量速度下,传热系数在不同的方向和加热配置之间显示出显着的变化,但对800 kg / m〜2 s以上的方向变得不敏感,证明围绕该质量速度的惯性可有效地消除重力效应。对于低质量速度,垂直向上流动和垂直向下流动的压降相当,但大于水平流动。但是,对于所有方向,在高质量速度下都可以获得相当相等的压降。总的来说,这项研究证明重力对两相压降和两相传热的影响主要由质量速度决定,而在较小程度上由入口质量决定。

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