Heat Exchanger Design and Optimization

Overview

The Shell and Tube Heat Exchanger is widely used in high -pressure industrial applications such as petrochemical processing and offshore oil rigs. This study examines the thermal performance of an HT33 Shell and Tube Heat Exchanger Unit (Armfield, Inc.) with a 20,000 mm² heat transfer surface area, 144 mm heat transfer length, and 44.45 mm shell diameter housing seven smaller tubes (6.35 mm each) with six semicircular baffles. A countercurrent flow configuration was used, with cold water circulating through the shell while hot water flowed in the opposite direction at controlled velocities. The primary objective is to analyze how varying hot fluid velocities impact heat exchanger effectiveness. Experimental testing and computational modeling using ANSYS Fluent’s finite volume method (FVM) were conducted. Results showed that increasing hot flu id velocities improved heat transfer effectiveness by up to 7%. However, overall effectiveness remained low (0.22) due to potential pressure stabilization issues, fouling, insulation inefficiencies, and structural constraints. CFD simulations predicted an effectiveness of 0.28, revealing a 27% discrepancy between experimental and simulated results. To enhance heat transfer, two geometric design modifications were proposed. The first incorporated 15 radially placed straight fins, increasing the heat transfer surface area by up to 250% and potentially improving effectiveness to 0.50. The second introdu ced U-shaped tubes embedded with similar fins, further expanding the surface area by 300%, potentially achieving even greater effectiveness. Ongoing ANSYS Fluent and MATLAB simulations aim to validate these designs for industrial applications, optimizing h eat exchanger performance and thermal efficiency.

Competition history

• JSHS 2025 Category not listed

Resources

• National JSHS abstract book ↗

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