A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow

This paper presents the numerical study on the two-dimensional forced convection heat transfer for staggered tube banks in cross flow under incompressible, steady-state conditions. This system is solved on the body fitted coordinates (BFC) using the finite difference method (FDM)for the flow over a...

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Main Authors: Tahseen, Tahseen Ahmad, M., Ishak, M. M., Rahman
Format: Conference or Workshop Item
Language:English
Published: Universiti Malaysia Pahang 2011
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Online Access:http://umpir.ump.edu.my/id/eprint/3800/1/FKM-2011-tahseen-numerical_study_of.pdf
http://umpir.ump.edu.my/id/eprint/3800/
https://www.researchgate.net/profile/Tahseen_Ahmad_Tahseen/publication/255990885_A_numerical_study_of_forced_convection_heat_transfer_for_staggered_tube_banks_in_cross-flow/links/02e7e5214b7e21758c000000/A-numerical-study-of-forced-convection-heat-transfe
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spelling my.ump.umpir.38002018-02-14T06:08:17Z http://umpir.ump.edu.my/id/eprint/3800/ A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow Tahseen, Tahseen Ahmad M., Ishak M. M., Rahman TJ Mechanical engineering and machinery This paper presents the numerical study on the two-dimensional forced convection heat transfer for staggered tube banks in cross flow under incompressible, steady-state conditions. This system is solved on the body fitted coordinates (BFC) using the finite difference method (FDM)for the flow over a bundle of cylindrical tubes. The constant heat flux is imposed on the surface of the tubes as the thermal boundary condition. The type of the arrangement is considered a staggered of tubes. The longitudinal pitch to tube diameter ratios (ST/D) of 1.25, 1.5 and 2 are also considered. Reynolds numbers are varied from 25 to 250 and Prandtl number is taken as 0.71. Velocity field vectors and temperature contours, local and average Nusselt numbers were analysed in this paper. It can be seen that the predicted results are good agreements with previous experimental and numerical results. The obtained results show that the heat transfer rate increases with decreases of the step to the longitudinal tube diameter. The local heat transfer strongly depends on the Reynolds number. It tends to obtain the highest values at the surface opposite to the direction of flow. The heat transfer rate is insignificant in the areas of recycling. Universiti Malaysia Pahang 2011-12-05 Conference or Workshop Item PeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/3800/1/FKM-2011-tahseen-numerical_study_of.pdf Tahseen, Tahseen Ahmad and M., Ishak and M. M., Rahman (2011) A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow. In: 1st International Conference on Mechanical Engineering Research, 5-7 Disember 2011 , Kuantan, Pahang Darul Makmur. pp. 216-227.. https://www.researchgate.net/profile/Tahseen_Ahmad_Tahseen/publication/255990885_A_numerical_study_of_forced_convection_heat_transfer_for_staggered_tube_banks_in_cross-flow/links/02e7e5214b7e21758c000000/A-numerical-study-of-forced-convection-heat-transfe
institution Universiti Malaysia Pahang
building UMP Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang
content_source UMP Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic TJ Mechanical engineering and machinery
spellingShingle TJ Mechanical engineering and machinery
Tahseen, Tahseen Ahmad
M., Ishak
M. M., Rahman
A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow
description This paper presents the numerical study on the two-dimensional forced convection heat transfer for staggered tube banks in cross flow under incompressible, steady-state conditions. This system is solved on the body fitted coordinates (BFC) using the finite difference method (FDM)for the flow over a bundle of cylindrical tubes. The constant heat flux is imposed on the surface of the tubes as the thermal boundary condition. The type of the arrangement is considered a staggered of tubes. The longitudinal pitch to tube diameter ratios (ST/D) of 1.25, 1.5 and 2 are also considered. Reynolds numbers are varied from 25 to 250 and Prandtl number is taken as 0.71. Velocity field vectors and temperature contours, local and average Nusselt numbers were analysed in this paper. It can be seen that the predicted results are good agreements with previous experimental and numerical results. The obtained results show that the heat transfer rate increases with decreases of the step to the longitudinal tube diameter. The local heat transfer strongly depends on the Reynolds number. It tends to obtain the highest values at the surface opposite to the direction of flow. The heat transfer rate is insignificant in the areas of recycling.
format Conference or Workshop Item
author Tahseen, Tahseen Ahmad
M., Ishak
M. M., Rahman
author_facet Tahseen, Tahseen Ahmad
M., Ishak
M. M., Rahman
author_sort Tahseen, Tahseen Ahmad
title A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow
title_short A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow
title_full A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow
title_fullStr A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow
title_full_unstemmed A Numerical Study of Forced Convection Heat Transfer for Staggered Tube Banks in Cross-Flow
title_sort numerical study of forced convection heat transfer for staggered tube banks in cross-flow
publisher Universiti Malaysia Pahang
publishDate 2011
url http://umpir.ump.edu.my/id/eprint/3800/1/FKM-2011-tahseen-numerical_study_of.pdf
http://umpir.ump.edu.my/id/eprint/3800/
https://www.researchgate.net/profile/Tahseen_Ahmad_Tahseen/publication/255990885_A_numerical_study_of_forced_convection_heat_transfer_for_staggered_tube_banks_in_cross-flow/links/02e7e5214b7e21758c000000/A-numerical-study-of-forced-convection-heat-transfe
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