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Flow boiling heat transfer in minichannels at high saturation temperatures: Part Ⅰ - Experimental investigation and analysis of the heat transfer mechanisms

机译:高饱和温度下微通道中的流沸腾传热:第一部分-传热机理的实验研究与分析

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This paper presents new experimental data concerning flow boiling heat transfer in minichannel at high saturation temperatures. The experimental data were obtained in a horizontal 3.00 mm inner diameter stainless steel tube with R-245fa as working fluid. The mass velocity ranges from 100 to 1500 kg/m~2 s, the heat flux varies from 10 to 50 kW/m~2 and the inlet vapor quality from 0 to 1. This experimental work is characterized by a saturation temperature ranging from 100 ℃ to 120 ℃. Row boiling heat transfer coefficients in these conditions have not been reported in the open literature so far. Four flow patterns are likely to appear in these conditions: intermittent flow, annular flow, dryout flow and mist flow regimes. The kind of flow pattern has a major influence on the heat transfer mechanisms. The influence of the mass velocity and the heat flux was investigated to identify the dominant heat transfer mechanisms. At high saturation temperatures, the experimental results clearly show the dominance of nucleate boiling over a wide range of vapor quality.
机译:本文提出了有关高饱和温度下微通道内流沸腾传热的新实验数据。在水平内径为3.00 mm的不锈钢管中以R-245fa作为工作流体获得了实验数据。质量速度范围从100到1500 kg / m〜2 s,热通量从10到50 kW / m〜2不等,入口蒸汽质量从0到1。该实验工作的特征是饱和温度为100 ℃至120℃。在这些条件下的行沸腾传热系数迄今尚未在公开文献中报道。在这些条件下可能会出现四种流动形式:间歇流动,环形流动,变干流动和雾流状态。流动方式的种类对传热机理有重要影响。研究了质量速度和热通量的影响,以确定主要的传热机理。在高饱和温度下,实验结果清楚地表明,在广泛的蒸汽质量范围内,核沸腾占主导地位。

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