Numerical investigation of the performance of perforated baffles in a plate-fin heat exchanger
The present paper is a numerical investigation on the performance of perforated baffles in a plate-fin heat exchanger. Two types of perforations are studied, namely the circular and elliptical shapes. Values of heat transfer coefficient, pressure drop, and thermal performance factor are determined f...
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VINCA Institute of Nuclear Sciences
2021-01-01
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doaj-4207fe3638014920944dfd061395d8db2021-09-24T09:48:23ZengVINCA Institute of Nuclear SciencesThermal Science0354-98362334-71632021-01-01255 Part B3629364110.2298/TSCI190316090A0354-98362000090ANumerical investigation of the performance of perforated baffles in a plate-fin heat exchangerAmeur Houari0Sahel Djamel1Menni Younes2Department of Technology, University Centre of Naama (Ctr Univ Naama), AlgeriaDepartment of Technical Sciences, University Amar Thilidji of Laghouat, AlgeriaUnite of Research on Materials and Renewable Energies - URMER, Department of Physics, Abou Bekr Belkaid University, Tlemcen, AlgeriaThe present paper is a numerical investigation on the performance of perforated baffles in a plate-fin heat exchanger. Two types of perforations are studied, namely the circular and elliptical shapes. Values of heat transfer coefficient, pressure drop, and thermal performance factor are determined for both cases and compared with those for a smooth channel. Also, the flow fields and heat transfer characteristics are determined for different fluids and various Reynolds numbers. The working fluids are complex, non-Newtonian and have an inelastic shear thinning behavior. The obtained results showed a good enhancement in the thermal performance factor by the suggested design in baffles. In the case of low viscous fluids, the elliptical perforated baffle performs better (by about 63.4%) than the circular one for all values of Reynolds number. But for highly viscous fluids, the elliptical perforation shows higher thermal performance than the circular hole by about 25% for low Reynolds numbers and 27% for high Reynolds numbers. The overall thermal performance factors are about 1.55 and 1.74 for the circular and elliptical perforations, respectively.http://www.doiserbia.nb.rs/img/doi/0354-9836/2021/0354-98362000090A.pdfplate-fin heat exchangerperforated bafflenon-newtonian fluidshear thinning fluidcfd |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Ameur Houari Sahel Djamel Menni Younes |
spellingShingle |
Ameur Houari Sahel Djamel Menni Younes Numerical investigation of the performance of perforated baffles in a plate-fin heat exchanger Thermal Science plate-fin heat exchanger perforated baffle non-newtonian fluid shear thinning fluid cfd |
author_facet |
Ameur Houari Sahel Djamel Menni Younes |
author_sort |
Ameur Houari |
title |
Numerical investigation of the performance of perforated baffles in a plate-fin heat exchanger |
title_short |
Numerical investigation of the performance of perforated baffles in a plate-fin heat exchanger |
title_full |
Numerical investigation of the performance of perforated baffles in a plate-fin heat exchanger |
title_fullStr |
Numerical investigation of the performance of perforated baffles in a plate-fin heat exchanger |
title_full_unstemmed |
Numerical investigation of the performance of perforated baffles in a plate-fin heat exchanger |
title_sort |
numerical investigation of the performance of perforated baffles in a plate-fin heat exchanger |
publisher |
VINCA Institute of Nuclear Sciences |
series |
Thermal Science |
issn |
0354-9836 2334-7163 |
publishDate |
2021-01-01 |
description |
The present paper is a numerical investigation on the performance of perforated baffles in a plate-fin heat exchanger. Two types of perforations are studied, namely the circular and elliptical shapes. Values of heat transfer coefficient, pressure drop, and thermal performance factor are determined for both cases and compared with those for a smooth channel. Also, the flow fields and heat transfer characteristics are determined for different fluids and various Reynolds numbers. The working fluids are complex, non-Newtonian and have an inelastic shear thinning behavior. The obtained results showed a good enhancement in the thermal performance factor by the suggested design in baffles. In the case of low viscous fluids, the elliptical perforated baffle performs better (by about 63.4%) than the circular one for all values of Reynolds number. But for highly viscous fluids, the elliptical perforation shows higher thermal performance than the circular hole by about 25% for low Reynolds numbers and 27% for high Reynolds numbers. The overall thermal performance factors are about 1.55 and 1.74 for the circular and elliptical perforations, respectively. |
topic |
plate-fin heat exchanger perforated baffle non-newtonian fluid shear thinning fluid cfd |
url |
http://www.doiserbia.nb.rs/img/doi/0354-9836/2021/0354-98362000090A.pdf |
work_keys_str_mv |
AT ameurhouari numericalinvestigationoftheperformanceofperforatedbafflesinaplatefinheatexchanger AT saheldjamel numericalinvestigationoftheperformanceofperforatedbafflesinaplatefinheatexchanger AT menniyounes numericalinvestigationoftheperformanceofperforatedbafflesinaplatefinheatexchanger |
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