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首页> 外文期刊>International Journal of Heat and Mass Transfer >Phenomenological correlations for two phase heat transfer and pressure drop performance of electrohydrodynamic horizontal convective boiling of dielectric fluids
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Phenomenological correlations for two phase heat transfer and pressure drop performance of electrohydrodynamic horizontal convective boiling of dielectric fluids

机译:电介质流体动力水平对流沸腾的两相传热与压降性能的现象学相关性

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摘要

EHD is an active heat transfer enhancement technique for convective boiling or condensing dielectric fluids whose performance varies widely in the literature for even the same geometry and fluids. As such, the performance of EHD convective boiling devices remains largely unpredictable. Two empirical EHD convective boiling heat transfer coefficient correlations exist in the literature with good performance when compared to their exact test dataset and geometry, however they have been shown to have poor correlations in predicting the performance for external test datasets.In this paper, a phenomenological approach is taken in the development of a new EHD convective boiling heat transfer coefficient correlation and a novel EHD convective boiling pressure drop correlation. The performance correlations are based on widely-used free-field convective boiling correlations for heat transfer coefficient and pressure drop with phenomenological enhancement factors based on the two phase flow pattern as predicted using the EHD two phase flow pattern map which accounts for the effect of electric field strength on flow pattern redistribution, as described in a previously published paper (Nangle-Smith and Cotton, 2018).A review of the EHD convective boiling experimental literature was conducted to determine confounding factors that can impact the large variance in the reported performance. Flow pattern and applied heat flux were identified as common parameters not maintained constant in the experimental data. Two data sets, including data from the present study, in which flow pattern and applied heat flux are maintained constant were used in the development of the performance correlations.Considerable improvement over previous EHD convective boiling performance correlations was found both in error and the physical significance of coefficients. The correlations were developed for thermodynamic qualities in the range of 20-60% below the onset of dryout or mist flow patterns and for applied heat fluxes 30 kIN/m(2). Furthermore, test conditions in this study were chosen to focus on the dielectrophoretic effect and therefore studies with significant electrophoresis were not included. Thus, the correlation is limited to positive applied voltages, saturated flow boiling conditions, and field strengths below the onset of charge injection. The authors recommend this approach for EHD two phase performance correlation development as it is more mechanistic, is analogous to the state-of-the-art approaches for free-field two phase performance, and is likely to yield more accurate models as more experimental data becomes available. Crown Copyright (C) 2018 Published by Elsevier Ltd. All rights reserved.
机译:EHD是一种用于对流沸腾或冷凝介电流体的主动传热增强技术,即使对于相同的几何形状和流体,其性能在文献中也有很大差异。因此,EHD对流沸腾装置的性能仍然很难预测。与确切的测试数据集和几何形状相比,文献中存在两个具有良好性能的经验EHD对流沸腾传热系数相关性,但是已证明它们在预测外部测试数据集的性能方面具有较弱的相关性。在开发新的EHD对流沸腾传热系数相关性和新型EHD对流沸腾压降相关性时,采用了这种方法。性能相关性是基于广泛使用的自由场对流沸腾相关性,其中基于热流两相流模式图预测的两相流模式,基于两相流模式的传热系数和压降与现象学增强因子,这考虑了电的影响如先前发表的论文(Nangle-Smith and Cotton,2018)中所述,场强对流型重新分布的影响进行了回顾,对EHD对流沸腾实验文献进行了研究,以确定可能影响所报告性能大差异的混杂因素。流动模式和施加的热通量被确定为实验数据中未保持恒定的常用参数。在建立性能相关性时使用了两个数据集,其中包括来自本研究的数据,其中流动模式和所施加的热通量保持恒定。在以前的EHD对流沸腾性能相关性方面发现了相当大的改进,无论是在误差上还是在物理意义上的系数。相关性是针对低于干燥或雾状流态开始20-60%范围内的热力学质量以及施加的热通量<30 kIN / m(2)而建立的。此外,选择本研究中的测试条件来关注介电泳效应,因此不包括具有重大电泳作用的研究。因此,相关仅限于正的施加电压,饱和流沸腾条件和低于电荷注入开始的场强。作者推荐这种方法用于EHD两相性能相关性开发,因为它更具机械性,类似于最新的自由场两相性能方法,并且随着更多的实验数据,可能会产生更准确的模型变得可用。 Crown版权所有(C)2018,由Elsevier Ltd.出版。保留所有权利。

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