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Experimental and numerical study on the heat transfer and flow characteristics in shell side of helically coiled tube heat exchanger based on multi-objective optimization

机译:基于多目标优化的螺旋管式换热器壳侧传热与流动特性的实验与数值研究

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摘要

Based on two-layer multi-objective optimization which is aimed at maximum performance evaluation criterion (PEC) and maximum field synergy number (Fc), the heat transfer and flow characteristics in shell side of helically coiled tube heat exchanger are investigated experimentally and numerically. The sensitivity analysis, univariate analysis and response surface analysis are conducted, in which, the selected working fluids are water and saturated vapor, and the transverse spacing (5), coiled radius (R), heat exchange tube diameter (d) are set as the design variables. The results suggested that d significantly affects f and PEC, while, R and S comparatively small, and for Nu, R is larger, whereas the difference between the three is small. The optimal structure for a Reynolds number from 5000 to 40,000 is that: d = 8 mm, R = 50 mm, S = 20 mm or 21 mm. Compared with the initial structure under the same working condition, the Fc based on the field synergy principle (FSP) indicates the comprehensive performance is improved by 36.84%, and PEC shows 33.42% improvement in the comprehensive performance. The fitting correlations of Nu and f in shell side of helically coiled tube heat exchanger fitted by the numerical simulation data are well consistent with the experimental data. (C) 2019 Elsevier Ltd. All rights reserved.
机译:基于针对最大性能评估标准(PEC)和最大场协同数(Fc)的两层多目标优化,对螺旋盘管换热器壳侧的传热和流动特性进行了实验和数值研究。进行敏感性分析,单变量分析和响应面分析,其中选择的工作流体为水和饱和蒸汽,并将横向间距(5),盘绕半径(R),换热管直径(d)设置为设计变量。结果表明,d显着影响f和PEC,而R和S相对较小,对于Nu,R较大,而两者之间的差异较小。雷诺数从5000到40,000的最佳结构是:d = 8毫米,R = 50毫米,S = 20毫米或21毫米。与相同工作条件下的初始结构相比,基于场协同原理(FSP)的Fc表明综合性能提高了36.84%,PEC表明综合性能提高了33.42%。数值模拟数据拟合的螺旋盘管换热器壳侧Nu和f的拟合相关性与实验数据吻合良好。 (C)2019 Elsevier Ltd.保留所有权利。

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