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A scale analysis model for film boiling heat transfer on a vertical flat plate with wide applicability

机译:垂直平板上薄膜沸腾传热的尺度分析模型

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A model has been developed in present work, for a vertical flat plate under film boiling condition, based on scale analysis. The saturated and subcooled film boiling have been analyzed from heat and mass transfer consideration and appropriate vaporization criteria. The model takes care of natural convection and forced convection mode of heat transfer for subcooled case, while the saturated film boiling is treated with an assisting convection mode. The interfacial wave length is incorporated into the length scale and the effect of radiation heat transfer is accounted in the model. Expressions for Nusselt number have been developed for different situations. The present model recovers the Bromley scale for natural convection under saturated condition. The heat transfer characteristic is shown for relevant non-dimensional numbers pertaining to film boiling for various cases. A wide set of existing experimental data with ranges of wall superheat 260-1200 ℃, liquid subcooling 0-50 ℃ and flow velocity 0-2.65 m/s have been systematically utilized to arrive at the model closure.
机译:在当前的工作中,已经基于比例分析为膜沸腾条件下的垂直平板开发了一个模型。从传热和传质的考虑以及适当的汽化标准对饱和和过冷的膜沸腾进行了分析。该模型考虑了过冷情况下的自然对流和强制对流传热模式,而饱和膜沸腾则采用辅助对流模式进行处理。将界面波长纳入长度尺度,并在模型中考虑了辐射传热的影响。已针对不同情况开发了Nusselt数的表达式。本模型恢复了在饱和条件下自然对流的Bromley标度。对于在各种情况下与膜沸腾有关的相关无量纲数示出了传热特性。系统地利用了大量现有的实验数据,壁过热度范围为260-1200℃,液体过冷度为0-50℃,流速为0-2.65 m / s,以达到模型闭合。

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