Determining of the thermo-hydraulic characteristics and exergy analysis of a triple helical tube with inner twisted tube

IF 3.8 3区 工程技术 Q3 ENERGY & FUELS
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Abstract

An innovative technique to enhance heat transfer as a passive method was investigated. The combination of the twisted tube and helical coil to increase the swirl intensity is presented. The current investigation showed experimentally and numerically the exergy and thermal performance analysis of a new design of a triple tube design called a triple helical tube with inner twisted tube, THTITT. The new design is a modified design of a double helical tube with inner twisted tube, DHTITT which is created by twisting the inner tube. Besides the benefits of adding the third fluid to DHTITT that achieve extra contact surface area per unit length between the intermediate tube and the new passage in the outer tube. In which expected to enhance the temperature gradient between the three fluids and consequently, the thermal characteristics augment occurred. The twisted tube increased the intensity of the swirl flow and more intense disturbance of the fluid in the tube occurred. A 3d CFD model was established to get more insight at a level of detail not always available in the experiment. The effects of twisted pitch ratio, ξ hydraulic diameter, ω, helical coil torsion, α, helical coil inclination angle, φ, as well as Dean number, NDn, h were explored. Four groups of test specimens include various ξ of 5.32, 7.97, and ∞, various ω of 3.8, 6.8, and 9.9 mm, various α of 0.068, 0.095, and 0.121, and various φ of 0°, 45°, and 90° were established, manufactured and examined in this investigation. The investigation covered Reynolds number, NRe,h, for a range of 2450:29300 corresponding to Dean number, NDn, h, for a range of 570:4800. The results showed a higher Nusselt number, NNu, h, of THTITT compared to DHTITT by 61.8 %%, while the increase in fh is approximately negligible. Also, by decreasing ξ from ∞ to 5.32 increases NNu, h by 33.4 %, with an increase in friction factor, fh by 57.6 %. Furthermore, with a decreasing ω from 9.9 mm to 3.8 mm, a significant increase in NNu, h occurs by 20.6 %, at the expense of increasing fh by 36.4 %. In addition, with decreasing α from 0.121 to 0.068, a significant increase in NNu, h occurs by 27.6 %, at the expense of increasing fh by 17.1 %. Finally, the THTITT decreases the heat loss (exergy destruction) between the hot and cold fluids. New correlations to predict NNu,h, and fh are presented.

带内扭曲管的三螺旋管的热液压特性测定和能耗分析
研究了一种作为被动方法增强传热的创新技术。研究介绍了扭曲管和螺旋线圈的组合,以增加漩涡强度。目前的研究通过实验和数值分析,展示了一种新设计的三管设计,即带内扭曲管的三螺旋管(THTITT)。这种新设计是带内扭曲管的双螺旋管(DHTITT)的改进设计,通过扭曲内管而产生。在 DHTITT 中加入第三种流体的好处是,在中间管和外管中的新通道之间实现了单位长度上的额外接触表面积。这有望增强三种流体之间的温度梯度,从而提高热特性。扭曲的管子增加了漩涡流的强度,管内流体受到更强烈的扰动。我们建立了一个 3D CFD 模型,以便更深入地了解实验中无法获得的细节。研究了扭曲节距比、ξ 液压直径、ω、螺旋线圈扭转、α、螺旋线圈倾斜角、φ 以及迪安数 NDn、h 的影响。本次研究建立、制造和检验了四组试样,包括 5.32、7.97 和 ∞ 的不同 ξ,3.8、6.8 和 9.9 mm 的不同 ω,0.068、0.095 和 0.121 的不同 α,以及 0°、45° 和 90° 的不同 φ。研究范围包括雷诺数 NRe,h 在 2450:29300 之间的变化,以及迪安数 NDn,h 在 570:4800 之间的变化。结果表明,THTITT 的努塞尔特数 NNu, h 比 DHTITT 高 61.8%,而 fh 的增加几乎可以忽略不计。此外,将 ξ 从 ∞ 减小到 5.32 时,NNu, h 增加了 33.4%,摩擦因数 fh 增加了 57.6%。此外,随着 ω 从 9.9 毫米减小到 3.8 毫米,NNu, h 显著增加了 20.6%,但摩擦因数 fh 增加了 36.4%。此外,随着 α 从 0.121 减小到 0.068,NNu, h 显著增加了 27.6%,而 fh 却增加了 17.1%。最后,THTITT 减少了冷热流体之间的热损失(放能破坏)。本文介绍了预测 NNu、h 和 fh 的新相关性。
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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来源期刊
CiteScore
7.80
自引率
9.30%
发文量
408
审稿时长
49 days
期刊介绍: Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.
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