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首页> 外文期刊>Journal of Heat Transfer >Thermohydraulic Behavior of the Liquid-Vapor Flow in the Receiver Tube of a Solar Parabolic Trough Collector
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Thermohydraulic Behavior of the Liquid-Vapor Flow in the Receiver Tube of a Solar Parabolic Trough Collector

机译:太阳能抛物线槽收集器接收管中液体蒸汽流动的热液态行为

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摘要

Liquid-vapor flows are present in many industrial applications. In particular, in the solar field, these flows are encountered in the new generations of solar parabolic trough collectors with direct steam generation (PTCs-DSG). In this technical brief, we compare the two-phase convective transfer and the pressure drop models in the PTC-DSG. The results show that the heat exchange coefficients estimated by Chen-Cooper, Shah, Gungor-Winterton, and Kandlikar models have same trend with difference between them. However, the models of Liu-Winterton and Steiner-Taborek seem inappropriate due to the decrease in the exchange coefficient for moderate and high steam qualities. In addition, a comparison of the models describing pressure drops with experimental data of literature was carried out. The results show that the pressure decreases as the steam quality increases and the differences between these models remain small. Friedel's model is the closest to the experiment for high inlet pressures and flow rates, while Chisholm's model gives the best prediction of the pressure drop for low inlet conditions. Effect analysis of inlet conditions shows that the increase in inlet water mass flow and decrease in pressure favor convective heat transfer. The variation of heat flux on tube wall does not affect the convective boiling heat coefficient evaluated by the Chen-Copper model, whereas it influences the calculating coefficient by Gungor-Winterton model for high heat flux and particularly for low steam qualities. Pressure drops are higher at high flow rates and low pressures.
机译:液体蒸汽流量存在于许多工业应用中。特别是,在太阳能领域,这些流量在具有直接蒸汽发生(PTCS-DSG)的太阳能抛物线收集器中遇到这些流量。在本技术简介中,我们比较了PTC-DSG中的两相对流转移和压力下降模型。结果表明,Chen-Cooper,Shah,Gungor-Winterton和Kandlikar模型估计的热交换系数具有相同的趋势与它们之间的差异相同。然而,由于对中等和高蒸汽质量的交换系数的减少,刘温顿和施坦纳 - 塔比尔克的模型似乎不恰当。此外,进行了描述具有文献实验数据的压降模型的比较。结果表明,随着蒸汽质量的增加,这些模型之间的差异仍然很小,压力降低。 Friedel的模型是最接近高入口压力和流速的实验,而Chisholm的模型可以最佳地预测低入口条件的压降。入口条件的效果分析表明入口水质流量的增加和压力减少对流热传递。管壁上的热通量的变化不会影响由陈铜模型评估的对流沸腾热量系数,而它会影响GUNGOR-Winterton模型的计算系数,用于高热通量,特别是对于低蒸汽质量。高流量率和低压力下压降较高。

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  • 来源
    《Journal of Heat Transfer》 |2020年第10期|104501.1-104501.6|共6页
  • 作者

    Sara Sallam; Mohamed Taqi;

  • 作者单位

    Laboratoire d'Ingenierie et Materiaux Faculte des Sciences Ben M'sik Hassan Ⅱ University of Casablanca Avenue Driss El Haiti Sidi Othman Casablanca B.P. 7955 Morocco;

    Laboratoire d'Ingenierie et Materiaux Faculte des Sciences Ben M'sik Hassan Ⅱ University of Casablanca Avenue Driss El Harti Sidi Othman Casablanca B.P. 7955 Morocco;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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