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Design of Shell and Tube Heat Exchanger Using MATLAB and Finding the Steady State Time Using Energy Balance Equation

机译:基于MATLAB的壳管换热器设计及能量平衡方程求稳态时间。

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摘要

Design of shell and tube heat exchangers are done by formulating a standard procedure where the parameters required for building a HX is calculated using numerical method until the dimensions satisfy the condition for maximum overall heat transfer coefficient, this is done using a MATLAB code in which the calculations are iterated by varying the TEMA specified values for tube length and tube outer diameter. The output of this calculation is proposed to be the effective parameters for design of shell and tube heat exchanger for given boundary conditions. Energy balance over the heat exchanger for the designed HX was completed using partial differential equations, which was solved using second order Runge-Kutta method. Since Runge-Kutta method is very robust and efficient, so thermal diffusion term is not included in the energy balance equation. By plotting a temperature v/s tube length graph in MATLAB using the energy balance differential equation and analyzing the same, time required for the shell and tube heat exchanger to reach a steady state condition is obtained. The present work proposes a standard steps to design and analyze the working and performance of a shell and tube heat exchanger.
机译:壳管式换热器的设计通过制定标准程序来完成,其中使用数值方法计算建造HX所需的参数,直到尺寸满足最大总传热系数的条件为止,这是使用MATLAB代码完成的,通过更改TEMA指定的管长度和管外径值来重复进行计算。在给定的边界条件下,该计算的输出被认为是管壳式换热器设计的有效参数。设计的HX的热交换器上的能量平衡使用偏微分方程完成,该方程使用二阶Runge-Kutta方法求解。由于Runge-Kutta方法非常健壮和高效,因此热扩散项不包括在能量平衡方程中。通过使用能量平衡微分方程在MATLAB中绘制温度v / s管长度图并对其进行分析,可以获得管壳式热交换器达到稳态条件所需的时间。本工作提出了设计和分析壳管式热交换器的工作和性能的标准步骤。

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