Numerical Investigation on Mitigation of Heat Transfer Deterioration of Supercritical CO2 Flow by Introducing Multiple Turbulators Along Helices in a Circular Tube

Hangfei Duan, G. Xie, Yuan Ma, Shulei Li
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Abstract

In order to effectively alleviate the heat transfer deterioration phenomenon of supercritical CO2 (S-CO2) in a vertical circular tube, explores the fluid hydraulic and thermal performance of multiple turbulator distributed along helices through a verified standard k-ω model. The effects of the pitch and the height of turbulators on flow characteristic and heat transfer are observed and analyzed in detail. With the increase of the height of turbulators, the heat transfer coefficient increases significantly. Besides, as the pitch decreases, the fluid re-circulation area behind each turbulator decreases, resulting in stronger mixing of swirling flow, which enhances turbulent kinetic energy of downstream fluid and weakens buoyancy force, thus mitigating heat transfer deterioration. The present results suggest that introducing multiple turbulators distributed along helices into circular tube can be a beneficial way to alleviate heat transfer deterioration and to enhance heat transfer of supercritical CO2 flow.
在圆管内沿螺旋引入多个紊流器缓解超临界CO2流动传热恶化的数值研究
为了有效缓解超临界CO2 (S-CO2)在垂直圆管内的传热恶化现象,通过验证的标准k-ω模型,探讨了沿螺旋分布的多个紊流器的流体水力和热性能。详细观察和分析了桨距和桨高对流动特性和换热的影响。随着扰流器高度的增加,换热系数显著增大。此外,随着桨距的减小,各紊流器后面的流体再循环面积减小,导致旋流混合更强,增强了下游流体的湍流动能,减弱了浮力,从而减轻了换热恶化。研究结果表明,在圆管内引入沿螺旋分布的多个紊流器可以有效地缓解超临界CO2流动的传热恶化,增强超临界CO2流动的换热能力。
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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