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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Suggestion of new correlations for the exergy efficiency and coefficient of exergy performance of annulus section of conically coiled tube-in-tube heat exchangers
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Suggestion of new correlations for the exergy efficiency and coefficient of exergy performance of annulus section of conically coiled tube-in-tube heat exchangers

机译:截然圆形管 - 管式热交换器环形截面截面截面型断路效率和变系数的新相关性建议

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In this study, the steady state heat transfer and fluid flow in the annulus section of tube-in-tube conically coiled heat exchanger (TTCCHE) is numerically investigated. The flow in the annulus is simulated using the Realizable K-ε turbulence model and validated by comparison with published Nusselt numbers. The effect of geometrical and operational parameters of the heat exchanger on the exergy characteristics of the annulus section is obtained. The results allowed for obtaining two correlations for estimation of the annulus section exergy efficiency and coefficient of exergy performance. Furthermore, it was found that the highest values of the turn number and the minimum values of the Reynolds number (d_(t,o)/d_(c,max)), (p/d_(c,max)), Prandtl number, tube diameter ratio and the cone angle in the studied range maximize the exergy efficiency and coefficient of exergy performance.
机译:在该研究中,在数值上研究了管 - 管圆周盘绕热交换器(TTCCHE)的环空部分中的稳态传热和流体流动。 使用可实现的K-ε湍流模型进行模拟环中的流程,并通过与已发表的培养数进行比较验证。 获得了热交换器的几何和操作参数对环形部分的漏洞特性的影响。 允许获得两个相关性,以估计环形部分的估计效率和漏洞性能系数。 此外,发现轮数的最高值和雷诺数的最小值(d_(t,o)/ d_(c,max)),(p / d_(c,max)),prandtl编号 ,管道直径比和研究范围内的锥角最大限度地提高了高度效率和漏洞性能系数。

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