Dimensional analysis applied to jacketed shell and tube heat exchangers modeling

Andrés A. Sánchez-Escalona, Yanan Camaraza-Medina, Yoalbys Retirado-Mediaceja, Ever Góngora-Leyva, Manuel Vega-Almaguer
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Abstract

Dimensional analysis was utilized on this research to establish a shortcut model for predicting hydrogen sulphide gas discharge temperature in jacketed shell and tube heat exchangers. Since the equipment belongs to an online industrial facility, the passive experimental method was applied. Selection of the heat transfer process parameters was followed by application of the Buckingham Pi-theorem and the repeating-variables technique. After formulation of the dimensionless groups, approximation of the explicit model equation was carried out through a least-squares multivariate linear regression. The model predictive ability performance was appraised by comparing predictions versus measured discharge temperatures, hence attaining a Pearson correlation of 97.5 %, a mean absolute error of 2.1 K, and 1.7 % maximum deviations. The explicit equation that was obtained is pertinent to studied heat exchangers, when 0.55 ≤ ṁ1 ≤ 0.60, 1.06 ≤ ṁ2 ≤ 1.09, and 0.22 ≤ ṁ3 ≤ 0.24 (fluids flowrate, kg/s). It can be used as an alternative calculation method for quick anticipation of the equipment performance, which overcomes computation of the overall heat transfer coefficients.
尺寸分析在夹套管壳式换热器建模中的应用
利用量纲分析方法,建立了套管壳式换热器硫化氢气体排放温度预测的快捷模型。由于该设备属于在线工业设备,故采用被动实验方法。采用Buckingham pi定理和重复变量技术对传热过程参数进行了选择。在建立无因次群后,通过最小二乘多元线性回归对显式模型方程进行近似。通过比较预测结果与实测放电温度,对模型的预测能力进行了评价,Pearson相关性为97.5%,平均绝对误差为2.1 K,最大偏差为1.7%。得到的显式方程与所研究的换热器有关,当流体流速,kg/s, 0.55≤ṁ1≤0.60,1.06≤ṁ2≤1.09,0.22≤ṁ3≤0.24时。它可以作为一种替代的计算方法,用于快速预测设备的性能,克服了计算总传热系数。
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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