Analysis of Heat Transfer in Shell and Tube Heat Exchanger (STHE) using Counter and Parallel Flow

Authors

  • Muhammad Danial Aiman Zaidi Mohd Yazid Universiti Tun Hussein Onn Malaysia Author
  • Nor Mazlana Main Universiti Tun Hussein Onn Malaysia Author

Keywords:

Heat Exchanger, Shell and Tube, Parallel Flow, Counter Flow, CFD analysis, Solidworks

Abstract

A heat exchanger is a device specifically engineered to enable the transfer of thermal energy between two fluids that have different temperatures. A shell and tube heat exchanger (STHE) is a widely used heat exchanger that facilitates the transfer of heat between a gas or liquid medium. The efficiency of heat exchangers is vital in the thermal industry. The objective of this study is to investigate the efficiency of shell and tube heat exchangers, with a particular focus on parallel and counter flow arrangements when two different fluids are utilized.  Design and simulations are conducted using SolidWorks2020 and computational fluid dynamics (CFD), taking into consideration operational parameters such as flow rates, inlet temperatures, fluid properties, boundary condition and others. The results reveal that counter flow produces a higher temperature difference, improving heat transfer efficiency near the outlet. However, calculated values indicate higher heat transfer in parallel flow, contradicting grapical results which is 86,073.65W for counter flow and 94,975.46W for parallel flow. This discrepancy may stem from various factors. The practical design adheres to Tubular Exchanger Manufacturers Association (TEMA) requirements, providing useful insights into the thermal efficiency of STHE.

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Published

17-10-2024

Issue

Section

Panel Loji (BDJ)

How to Cite

Zaidi Mohd Yazid, M. D. A., & Main, N. M. (2024). Analysis of Heat Transfer in Shell and Tube Heat Exchanger (STHE) using Counter and Parallel Flow. Research Progress in Mechanical and Manufacturing Engineering, 5(1), 460-468. https://publisher.uthm.edu.my/periodicals/index.php/rpmme/article/view/15805