The effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe

The effect of different inlet geometries on laminar air flow combined convection heat transfer inside a horizontal circular pipe has been experimentally investigated for Reynolds number range of 400-1600, and the Grashof number range from 3.12 � 105 to 1.72 � 106. The experimental setup consists of...

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Main Author: Mohammed H.A.
Other Authors: 15837504600
Format: Article
Published: 2023
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Air
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Institution: Universiti Tenaga Nasional
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spelling my.uniten.dspace-308542023-12-29T15:54:42Z The effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe Mohammed H.A. 15837504600 Combined convection Different inlet geometries Fully developed flow Heat exchangers applications Horizontal circular pipe Uniform wall heat flux Aerodynamics Air Alumina Bells Fluid dynamics Heat convection Heat exchangers Heat flux Heat transfer Heating equipment Laminar flow Mixed convection Nanofluidics Pipe Reynolds number Thermoanalysis Combined convection Different inlet geometries Fully developed flow Horizontal circular pipe Uniform wall heat flux Geometry The effect of different inlet geometries on laminar air flow combined convection heat transfer inside a horizontal circular pipe has been experimentally investigated for Reynolds number range of 400-1600, and the Grashof number range from 3.12 � 105 to 1.72 � 106. The experimental setup consists of an aluminum circular pipe as a heated section with 30 mm inside diameter and 900 mm heated length (L/D = 30) with different inlet geometries. A wall boundary heating condition of a uniform heat flux was imposed. The inlet configurations used in this paper are calming sections having the same inside diameter as the heated pipe but with variable lengths of Lcalm. = 600 mm (L/D = 20), Lcalm. = 1200 mm (L/D = 40), Lcalm. = 1800 mm (L/D = 60), Lcalm. = 2400 mm (L/D = 80), sharp-edged and bell-mouth. It was found that the surface temperature values for calming section length corresponding to (L/D = 80) were higher than other inlet geometries due to the lower mass flow rate and higher flow resistance. It was also observed that the Nusselt number values for bell-mouth inlet geometry were higher than other inlet geometries due to the differences in the average temperatures and densities of the air. The average heat transfer results were correlated with an empirical correlation in terms of dependent parameters of Grashof, Prandtl and Reynolds numbers. The proposed correlation was compared with available literature and it shows reasonable agreement. � 2008 Elsevier Ltd. All rights reserved. Final 2023-12-29T07:54:42Z 2023-12-29T07:54:42Z 2009 Article 10.1016/j.applthermaleng.2008.03.024 2-s2.0-55549123522 https://www.scopus.com/inward/record.uri?eid=2-s2.0-55549123522&doi=10.1016%2fj.applthermaleng.2008.03.024&partnerID=40&md5=b76bbbf3c9e2be2d56fd10590f130d7a https://irepository.uniten.edu.my/handle/123456789/30854 29 02/03/2023 581 590 Scopus
institution Universiti Tenaga Nasional
building UNITEN Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Tenaga Nasional
content_source UNITEN Institutional Repository
url_provider http://dspace.uniten.edu.my/
topic Combined convection
Different inlet geometries
Fully developed flow
Heat exchangers applications
Horizontal circular pipe
Uniform wall heat flux
Aerodynamics
Air
Alumina
Bells
Fluid dynamics
Heat convection
Heat exchangers
Heat flux
Heat transfer
Heating equipment
Laminar flow
Mixed convection
Nanofluidics
Pipe
Reynolds number
Thermoanalysis
Combined convection
Different inlet geometries
Fully developed flow
Horizontal circular pipe
Uniform wall heat flux
Geometry
spellingShingle Combined convection
Different inlet geometries
Fully developed flow
Heat exchangers applications
Horizontal circular pipe
Uniform wall heat flux
Aerodynamics
Air
Alumina
Bells
Fluid dynamics
Heat convection
Heat exchangers
Heat flux
Heat transfer
Heating equipment
Laminar flow
Mixed convection
Nanofluidics
Pipe
Reynolds number
Thermoanalysis
Combined convection
Different inlet geometries
Fully developed flow
Horizontal circular pipe
Uniform wall heat flux
Geometry
Mohammed H.A.
The effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe
description The effect of different inlet geometries on laminar air flow combined convection heat transfer inside a horizontal circular pipe has been experimentally investigated for Reynolds number range of 400-1600, and the Grashof number range from 3.12 � 105 to 1.72 � 106. The experimental setup consists of an aluminum circular pipe as a heated section with 30 mm inside diameter and 900 mm heated length (L/D = 30) with different inlet geometries. A wall boundary heating condition of a uniform heat flux was imposed. The inlet configurations used in this paper are calming sections having the same inside diameter as the heated pipe but with variable lengths of Lcalm. = 600 mm (L/D = 20), Lcalm. = 1200 mm (L/D = 40), Lcalm. = 1800 mm (L/D = 60), Lcalm. = 2400 mm (L/D = 80), sharp-edged and bell-mouth. It was found that the surface temperature values for calming section length corresponding to (L/D = 80) were higher than other inlet geometries due to the lower mass flow rate and higher flow resistance. It was also observed that the Nusselt number values for bell-mouth inlet geometry were higher than other inlet geometries due to the differences in the average temperatures and densities of the air. The average heat transfer results were correlated with an empirical correlation in terms of dependent parameters of Grashof, Prandtl and Reynolds numbers. The proposed correlation was compared with available literature and it shows reasonable agreement. � 2008 Elsevier Ltd. All rights reserved.
author2 15837504600
author_facet 15837504600
Mohammed H.A.
format Article
author Mohammed H.A.
author_sort Mohammed H.A.
title The effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe
title_short The effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe
title_full The effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe
title_fullStr The effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe
title_full_unstemmed The effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe
title_sort effect of different inlet geometries on laminar flow combined convection heat transfer inside a horizontal circular pipe
publishDate 2023
_version_ 1806427416342560768