Modeling and Optimization of Shell and Tube Heat Exchanger in Treatment Unit of South Pars Fifth Refinery by Fluent Software
American Journal of Mechanical and Industrial Engineering
Volume 2, Issue 4, July 2017, Pages: 150-161
Received: Apr. 11, 2017;
Accepted: Apr. 21, 2017;
Published: Jul. 4, 2017
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Kazem Moaveni, Department of Mechanic, Dashtestan Branch, Islamic Azad University, Borazjan, Iran
Mehran Zarkesh, Department of Mechanic, Dashtestan Branch, Islamic Azad University, Borazjan, Iran
In this thesis, the numerical solution of navier stockes equations and turbulent equations have also been investigated in fluent software, to investigate baffle type change from cut off to helical in shell and tube heat exchanger. RNG K-ε turbulence model was used to perturbations modelling. The main objective of baffle changing in thesis is increasing propane temperature in pipes outlet. 4 heat exchanger type with different helical angles (35, 40, 45 and 50) compared with simple baffle type. Studies indicate that heat exchanger with helical angle of 50°, maximum outlet temperature of propane will result and have the maximum heat transfer rate in shell. Exchangers with helical angle of 40 degrees have the highest ratio h / Δp, which reflects the heat transfer rate to pressure drop ratio.
Modeling and Optimization of Shell and Tube Heat Exchanger in Treatment Unit of South Pars Fifth Refinery by Fluent Software, American Journal of Mechanical and Industrial Engineering.
Vol. 2, No. 4,
2017, pp. 150-161.
Copyright © 2017 Authors retain the copyright of this article.
This article is an open access article distributed under the Creative Commons Attribution License (http://creativecommons.org/licenses/by/4.0/
) which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
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