Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach

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 volume method (FVM) for the flow ov...

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Main Authors: M., Ishak, Tahseen, Tahseen Ahmad, M. M., Rahman
Format: Article
Language:English
Published: Faculty Mechanical Engineering, UMP 2013
Subjects:
Online Access:http://umpir.ump.edu.my/id/eprint/3858/
http://umpir.ump.edu.my/id/eprint/3858/
http://umpir.ump.edu.my/id/eprint/3858/1/FKM-2013-Mahadzir-laminar_forced_convection.pdf
id ump-3858
recordtype eprints
spelling ump-38582018-01-25T03:06:33Z http://umpir.ump.edu.my/id/eprint/3858/ Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach M., Ishak Tahseen, Tahseen Ahmad 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 volume method (FVM) 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, temperature contours and 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. Faculty Mechanical Engineering, UMP 2013 Article PeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/3858/1/FKM-2013-Mahadzir-laminar_forced_convection.pdf M., Ishak and Tahseen, Tahseen Ahmad and M. M., Rahman (2013) Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach. Journal of Mechanical Engineering and Sciences (JMES), 4 (June 2). pp. 418-430. ISSN 2231-8380 (online) https://dl.dropboxusercontent.com/s/9jaw0290mxmbtbn/6_Tahseen%20et%20al.pdf?token_hash=AAFS6rxJfyoVGL4UYv0_RrrbhhPrTbTEmZlaRntXAXxfsg&disable_range=1
repository_type Digital Repository
institution_category Local University
institution Universiti Malaysia Pahang
building UMP Institutional Repository
collection Online Access
language English
topic TJ Mechanical engineering and machinery
spellingShingle TJ Mechanical engineering and machinery
M., Ishak
Tahseen, Tahseen Ahmad
M. M., Rahman
Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach
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 volume method (FVM) 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, temperature contours and 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 Article
author M., Ishak
Tahseen, Tahseen Ahmad
M. M., Rahman
author_facet M., Ishak
Tahseen, Tahseen Ahmad
M. M., Rahman
author_sort M., Ishak
title Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach
title_short Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach
title_full Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach
title_fullStr Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach
title_full_unstemmed Laminar Forced Convection Heat Transfer over Staggered Circular Tube Banks: A CFD Approach
title_sort laminar forced convection heat transfer over staggered circular tube banks: a cfd approach
publisher Faculty Mechanical Engineering, UMP
publishDate 2013
url http://umpir.ump.edu.my/id/eprint/3858/
http://umpir.ump.edu.my/id/eprint/3858/
http://umpir.ump.edu.my/id/eprint/3858/1/FKM-2013-Mahadzir-laminar_forced_convection.pdf
first_indexed 2023-09-18T21:58:25Z
last_indexed 2023-09-18T21:58:25Z
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