Heat Transfer for Forced Flow of Helium Gas in a Small Diameter Tube With Different Heated Length

Yushi Honjo, Feng Xu, Qiusheng Liu, M. Shibahara
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Abstract

As one of the cooling methods for the blanket in a fusion reactor, forced convection using helium gas has been considered as one of the promising candidates. In this study, in order to clarify the effect of tube length on heat transfer for forced flow of helium gas under various velocities and pressures, experiments on forced convection heat transfer for helium gas in a small diameter tube were conducted. A circular tube made of platinum with an inner diameter of 1.8 mm and a heated length of 50 mm was used in this experiment. The tube was heated with exponentially increasing heat inputs. As a result of the experiment, the heat transfer process can be considered in the quasi-steady state when the e-folding time is larger than about 1.5 s. In addition, the heat transfer coefficient increased with the increases in velocity and pressure. The heat transfer was also higher than that of conventional turbulent heat transfer correlation. By comparing with the experimental results of tube with different heated lengths, it was found that the heat transfer coefficients for the heated length of 50 mm were higher than those of the one with a length of 90 mm.
氦气在不同受热长度的小直径管内强制流动的换热特性
氦气强制对流作为核聚变堆包层冷却方法之一,已被认为是一种很有前途的冷却方法。在本研究中,为了明确不同流速和压力下管内长度对氦气强制对流换热的影响,进行了小直径管内氦气强制对流换热实验。实验采用内径为1.8 mm,加热长度为50 mm的铂制圆管。用指数增加的热输入加热管。实验结果表明,当电子折叠时间大于1.5 s左右时,传热过程可以考虑为准稳态。换热系数随流速和压力的增大而增大。换热系数也高于传统的湍流换热系数。通过对不同加热长度管的实验结果进行比较,发现加热长度为50 mm的管的换热系数高于加热长度为90 mm的管的换热系数。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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