Full Text Available

Note: Clicking the button above will open the full text document at the original institutional repository in a new window.

Heat transfer coefficients of smooth tubes in the turbulent flow regime

Dissertation (MEng)--University of Pretoria, 2015.

Saved in:
Bibliographic Details
Other Authors: Meyer, Josua P.
Format: Thesis
Language:English
Published: University of Pretoria 2015
Subjects:
Tags: Add Tag
No Tags, Be the first to tag this record!
_version_ 1867613608968454144
access_status_str Open Access
author2 Meyer, Josua P.
author_browse Meyer, Josua P.
author_facet Meyer, Josua P.
collection Thesis
dc_rights_str_mv © 2015 University of Pretoria. All rights reserved. The copyright in this work vests in the University of Pretoria. No part of this work may be reproduced or transmitted in any form or by any means, without the prior written permission of the University of Pretoria.
description Dissertation (MEng)--University of Pretoria, 2015.
format Thesis
id oai:repository.up.ac.za:2263/50858
institution University of Pretoria (South Africa)
language English
last_indexed 2026-06-10T12:38:51.633Z
license_str Other — see source repository
provenance_str_mv Harvested via OAI-PMH from UPSpace — University of Pretoria Institutional Repository
publishDate 2015
publishDateRange 2015
publishDateSort 2015
publisher University of Pretoria
publisherStr University of Pretoria
record_format dspace
source_str UPSpace — University of Pretoria Institutional Repository
spelling oai:repository.up.ac.za:2263/50858 Heat transfer coefficients of smooth tubes in the turbulent flow regime Meyer, Josua P. u24188647@tuks.co.za Coetzee, Nicole UCTD Heat Transfer Coefficients Smooth Tubes Turbulent Flow Heat Transfer Turbulent flow regime Engineering, built environment and information technology theses SDG-07 SDG-07: Affordable and clean energy Engineering, built environment and information technology theses SDG-09 SDG-09: Industry, innovation and infrastructure Engineering, built environment and information technology theses SDG-12 SDG-12: Responsible consumption and production Dissertation (MEng)--University of Pretoria, 2015. Several well-known equations are available in literature that can be used to determine the heat transfer coefficients of smooth tubes in the turbulent flow regime. When comparing the results of these equations they vary over a considerable range. Although in many cases it is assumed that the Gnielinski equation is one of the most accurate as it is the most recently developed correlation, the uncertainty of this equation has not be quantified as yet. Many of the equations have been developed using the data that was obtained from experimental testing as far back as 80 years ago. As more accurate instrumentation is available, it should be possible to collect more accurate data during experimental testing. The purpose of this study was threefold: to take accurate heat transfer measurements and to quantify the uncertainties of the Nusselt numbers as a function of Reynolds number; to compare the measured data with existing correlations and to develop an accurate Nusselt number correlation from the data. Experiments were conducted on two smooth circular tubes with a heat transfer length 3.75 m with inner tube diameters of 8.3 mm and 14.2 mm using water over a Reynolds number range of 10 000 to 220 000 and a Prandtl number range of 3.2 to 4. Surface roughness analysis was also performed to ensure the tubes can be considered as smooth tubes. Pressure drop measurements were also taken over tube lengths of 4.1 m as a function of Reynolds number. The experiments were conducted using a tube-in-tube heat exchanger with the hot water in the inner tube and the cold water in the annulus operating in a counter flow configuration. The friction factor values were determined from pressure drop measurements and the heat transfer coefficients were determined from the Wilson Plot method using temperature and mass flow rate measurements. The average uncertainties of the friction factors and Nusselt numbers were both less than 3%. The results were compared to the existing literature and it was found that at lower Reynolds numbers the Nusselt numbers deviated slightly to those of Gnielinski with the results comparing more closely with increasing Reynolds number. The friction factor results correlated well with that of Blasius. A new Nusselt number correlation, which is a function of Reynolds number, Prandtl number and friction factor, was developed. The equation predicted all the measured values within 3%. The equation is, however, limited in not taking into consideration large variations in fluid properties. tm2015 mi2025 Mechanical and Aeronautical Engineering MEng Unrestricted SDG-07: Affordable and clean energy SDG-09: Industry, innovation and infrastructure SDG-12: Responsible consumption and production 2015-11-25T09:53:59Z 2015-11-25T09:53:59Z 2015/09/01 2015 Dissertation Coetzee, N 2015, Heat transfer coefficients of smooth tubes in the turbulent flow regime, MEng Dissertation, University of Pretoria, Pretoria, viewed yymmdd <http://hdl.handle.net/2263/50858> S2015 http://hdl.handle.net/2263/50858 en © 2015 University of Pretoria. All rights reserved. The copyright in this work vests in the University of Pretoria. No part of this work may be reproduced or transmitted in any form or by any means, without the prior written permission of the University of Pretoria. application/pdf University of Pretoria
spellingShingle UCTD
Heat Transfer Coefficients
Smooth Tubes
Turbulent Flow
Heat Transfer
Turbulent flow regime
Engineering, built environment and information technology theses SDG-07
SDG-07: Affordable and clean energy
Engineering, built environment and information technology theses SDG-09
SDG-09: Industry, innovation and infrastructure
Engineering, built environment and information technology theses SDG-12
SDG-12: Responsible consumption and production
Heat transfer coefficients of smooth tubes in the turbulent flow regime
title Heat transfer coefficients of smooth tubes in the turbulent flow regime
title_full Heat transfer coefficients of smooth tubes in the turbulent flow regime
title_fullStr Heat transfer coefficients of smooth tubes in the turbulent flow regime
title_full_unstemmed Heat transfer coefficients of smooth tubes in the turbulent flow regime
title_short Heat transfer coefficients of smooth tubes in the turbulent flow regime
title_sort heat transfer coefficients of smooth tubes in the turbulent flow regime
topic UCTD
Heat Transfer Coefficients
Smooth Tubes
Turbulent Flow
Heat Transfer
Turbulent flow regime
Engineering, built environment and information technology theses SDG-07
SDG-07: Affordable and clean energy
Engineering, built environment and information technology theses SDG-09
SDG-09: Industry, innovation and infrastructure
Engineering, built environment and information technology theses SDG-12
SDG-12: Responsible consumption and production
url http://hdl.handle.net/2263/50858