{"title":"Analysis of Friction Factor of Two-Phase Flow in Helically Coiled Tubes","authors":"B. Jiang, Zhiwei Zhou, Y. Ji","doi":"10.1115/icone28-64356","DOIUrl":null,"url":null,"abstract":"\n With compact structure and enhanced heat transfer capacity, helical-coiled once through steam generators (HTSGs) are widely used in the small modular reactors (SMRs). Nevertheless, the inside centrifugal forces make the flow more complicated, and increase the frictional pressure drop, which is closely related to the dual test of alternating thermal stress and flow instability. Therefore, the analysis of the friction factor in helically coiled tubes is significant to the efficient and safe operation of HTSGs.\n While the friction factor of single-phase flow in helically coiled tubes was fully studied and extensive correlations have been validated by a large amount of experimental data, the friction factor of two-phase flow still lacks feasible prediction due to its much more complexity. The existed correlations of two-phase flow in helically coiled tubes are mostly based on specified experimental parameters, so the applicable range is limited. Few scholars have tried to extend these correlations to broader applicability, but the trivial applicable range is unsuitable for program development or engineering design, which needs an accurate prediction of friction factor in a wider range.\n In this paper, existing frictional pressure drop correlations are investigated. The accuracy of single-phase frictional pressure drop correlations is verified through the comparison of calculation results. Since the known experimental data cannot cover a wide range of parameters, two assumptions are proposed, and the rationality is verified through the existing experimental data and calculation analysis. Based on the two assumptions and calculation, a set of calculation correlations for frictional pressure drop of two-phase flow in helically coiled tubes are proposed. The accuracy of this calculation model is validated by experimental data. The scope of application of this model is: D / d = 15–100, P = 0.12–6.3MPa, G = 200–1500kg / m2s, which is sufficient to support the design and operation of steam generators and the development of the simulation programs.","PeriodicalId":108609,"journal":{"name":"Volume 4: Student Paper Competition","volume":"11 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2021-08-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Volume 4: Student Paper Competition","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1115/icone28-64356","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
With compact structure and enhanced heat transfer capacity, helical-coiled once through steam generators (HTSGs) are widely used in the small modular reactors (SMRs). Nevertheless, the inside centrifugal forces make the flow more complicated, and increase the frictional pressure drop, which is closely related to the dual test of alternating thermal stress and flow instability. Therefore, the analysis of the friction factor in helically coiled tubes is significant to the efficient and safe operation of HTSGs.
While the friction factor of single-phase flow in helically coiled tubes was fully studied and extensive correlations have been validated by a large amount of experimental data, the friction factor of two-phase flow still lacks feasible prediction due to its much more complexity. The existed correlations of two-phase flow in helically coiled tubes are mostly based on specified experimental parameters, so the applicable range is limited. Few scholars have tried to extend these correlations to broader applicability, but the trivial applicable range is unsuitable for program development or engineering design, which needs an accurate prediction of friction factor in a wider range.
In this paper, existing frictional pressure drop correlations are investigated. The accuracy of single-phase frictional pressure drop correlations is verified through the comparison of calculation results. Since the known experimental data cannot cover a wide range of parameters, two assumptions are proposed, and the rationality is verified through the existing experimental data and calculation analysis. Based on the two assumptions and calculation, a set of calculation correlations for frictional pressure drop of two-phase flow in helically coiled tubes are proposed. The accuracy of this calculation model is validated by experimental data. The scope of application of this model is: D / d = 15–100, P = 0.12–6.3MPa, G = 200–1500kg / m2s, which is sufficient to support the design and operation of steam generators and the development of the simulation programs.
螺旋盘管一次性蒸汽发生器(HTSGs)结构紧凑,传热能力强,在小型模块化反应堆(smr)中得到广泛应用。然而,内部离心力使流动更加复杂,增加了摩擦压降,这与交变热应力和流动不稳定性的双重试验密切相关。因此,螺旋盘管摩擦系数的分析对高温高温管高效安全运行具有重要意义。虽然螺旋螺旋管内单相流动的摩擦因数已经得到了充分的研究,大量的实验数据也验证了广泛的相关性,但由于两相流动的摩擦因数更为复杂,仍然缺乏可行的预测。现有的螺旋螺旋管内两相流的关系式多基于特定的实验参数,适用范围有限。很少有学者试图将这些相关性扩展到更广泛的适用性,但这种微小的适用范围并不适合程序开发或工程设计,这需要在更广泛的范围内准确预测摩擦系数。本文对已有的摩擦压降关系式进行了研究。通过计算结果的对比,验证了单相摩擦压降关系式的准确性。由于已知的实验数据不能涵盖广泛的参数范围,提出了两个假设,并通过现有的实验数据和计算分析验证了其合理性。在这两个假设和计算的基础上,提出了一套螺旋螺旋管内两相流摩擦压降的计算关系式。实验数据验证了该计算模型的准确性。该模型的适用范围为:D / D = 15-100, P = 0.12-6.3MPa, G = 200-1500kg / m2s,足以支持蒸汽发生器的设计、运行和仿真程序的开发。