Laminar convective heat transfer in helical tube with twisted tape insert

Tape insert has been commonly adopted as heat transfer enhancement method in a thermal system. Most studies dealing with tape insert have been focused on straight tube. Helical coil tube, on the other hand, has been proven to have higher heat transfer than straight tube. It is of interest to combine...

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Main Authors: Kurnia, J.C., Chaedir, B.A., Sasmito, A.P.
Format: Article
Published: Elsevier Ltd 2020
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85078036074&doi=10.1016%2fj.ijheatmasstransfer.2020.119309&partnerID=40&md5=bf7446b36162f8e20145d3636c207712
http://eprints.utp.edu.my/23210/
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spelling my.utp.eprints.232102021-08-19T06:09:14Z Laminar convective heat transfer in helical tube with twisted tape insert Kurnia, J.C. Chaedir, B.A. Sasmito, A.P. Tape insert has been commonly adopted as heat transfer enhancement method in a thermal system. Most studies dealing with tape insert have been focused on straight tube. Helical coil tube, on the other hand, has been proven to have higher heat transfer than straight tube. It is of interest to combine both enhancement methods and obtain the optimum heat transfer enhancement. The main objective of this study is, therefore, to numerically investigate flow behaviour and the corresponding heat transfer in helical tube with twisted tape insert subjected to constant wall temperature. A three-dimensional computational model is developed based on conservation equations of mass, momentum, and energy, and is validated against the established empirical correlations. Good agreement is achieved between the numerical prediction and the empirical correlation calculation within the considered range of Reynolds (Re=100�2000) and Dean Numbers (De=25�1200). The effects of twist ratio, inlet Reynolds number and wall temperature are evaluated and discussed in the light of numerical result. It is found that adding twisted tape insert in helical heat exchanger can enhance heat transfer performance by up to four times as compared to conventional straight tube heat exchanger, at a cost of higher frictional pressure drop. Lower twisting ratio gives rise to a higher heat transfer enhancement as it promotes higher secondary flow. At low Pr (air), heat transfer enhancement ratio increases as Re is increased; however, at high Pr (water), heat transfer enhancement ratio is higher at Re 500�1000. Finally, Nu and f correlations are developed to predict heat transfer and pressure drop for practical applications. © 2020 Elsevier Ltd 2020 Article NonPeerReviewed https://www.scopus.com/inward/record.uri?eid=2-s2.0-85078036074&doi=10.1016%2fj.ijheatmasstransfer.2020.119309&partnerID=40&md5=bf7446b36162f8e20145d3636c207712 Kurnia, J.C. and Chaedir, B.A. and Sasmito, A.P. (2020) Laminar convective heat transfer in helical tube with twisted tape insert. International Journal of Heat and Mass Transfer, 150 . http://eprints.utp.edu.my/23210/
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Institutional Repository
url_provider http://eprints.utp.edu.my/
description Tape insert has been commonly adopted as heat transfer enhancement method in a thermal system. Most studies dealing with tape insert have been focused on straight tube. Helical coil tube, on the other hand, has been proven to have higher heat transfer than straight tube. It is of interest to combine both enhancement methods and obtain the optimum heat transfer enhancement. The main objective of this study is, therefore, to numerically investigate flow behaviour and the corresponding heat transfer in helical tube with twisted tape insert subjected to constant wall temperature. A three-dimensional computational model is developed based on conservation equations of mass, momentum, and energy, and is validated against the established empirical correlations. Good agreement is achieved between the numerical prediction and the empirical correlation calculation within the considered range of Reynolds (Re=100�2000) and Dean Numbers (De=25�1200). The effects of twist ratio, inlet Reynolds number and wall temperature are evaluated and discussed in the light of numerical result. It is found that adding twisted tape insert in helical heat exchanger can enhance heat transfer performance by up to four times as compared to conventional straight tube heat exchanger, at a cost of higher frictional pressure drop. Lower twisting ratio gives rise to a higher heat transfer enhancement as it promotes higher secondary flow. At low Pr (air), heat transfer enhancement ratio increases as Re is increased; however, at high Pr (water), heat transfer enhancement ratio is higher at Re 500�1000. Finally, Nu and f correlations are developed to predict heat transfer and pressure drop for practical applications. © 2020
format Article
author Kurnia, J.C.
Chaedir, B.A.
Sasmito, A.P.
spellingShingle Kurnia, J.C.
Chaedir, B.A.
Sasmito, A.P.
Laminar convective heat transfer in helical tube with twisted tape insert
author_facet Kurnia, J.C.
Chaedir, B.A.
Sasmito, A.P.
author_sort Kurnia, J.C.
title Laminar convective heat transfer in helical tube with twisted tape insert
title_short Laminar convective heat transfer in helical tube with twisted tape insert
title_full Laminar convective heat transfer in helical tube with twisted tape insert
title_fullStr Laminar convective heat transfer in helical tube with twisted tape insert
title_full_unstemmed Laminar convective heat transfer in helical tube with twisted tape insert
title_sort laminar convective heat transfer in helical tube with twisted tape insert
publisher Elsevier Ltd
publishDate 2020
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85078036074&doi=10.1016%2fj.ijheatmasstransfer.2020.119309&partnerID=40&md5=bf7446b36162f8e20145d3636c207712
http://eprints.utp.edu.my/23210/
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