Loading…

Experimental investigation of heat transfer and pressure drop in serrated finned tube banks with staggered layouts

An experimental study was performed to investigate the heat transfer and pressure drop characteristics of serrated finned tube banks with staggered layouts. The influences of varied fin densities, transversal tube spacing and longitudinal tube spacing were presented. For a constant fin height, an in...

Full description

Saved in:
Bibliographic Details
Published in:Applied thermal engineering 2012-05, Vol.37, p.314-323
Main Authors: Ma, Youfu, Yuan, Yichao, Liu, Yuzheng, Hu, Xiaohong, Huang, Yan
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Items that cite this one
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by cdi_FETCH-LOGICAL-c363t-57096cbadfff7153aa7d3cdb7b2527a01477b81b7fd7f822dc3036e3c4d3bcb33
cites cdi_FETCH-LOGICAL-c363t-57096cbadfff7153aa7d3cdb7b2527a01477b81b7fd7f822dc3036e3c4d3bcb33
container_end_page 323
container_issue
container_start_page 314
container_title Applied thermal engineering
container_volume 37
creator Ma, Youfu
Yuan, Yichao
Liu, Yuzheng
Hu, Xiaohong
Huang, Yan
description An experimental study was performed to investigate the heat transfer and pressure drop characteristics of serrated finned tube banks with staggered layouts. The influences of varied fin densities, transversal tube spacing and longitudinal tube spacing were presented. For a constant fin height, an increase in the fin density resulted in an increase in the Euler number, and a gradual decrease in the Nusselt number was observed as the Reynolds number increased. An increase in the transversal tube spacing corresponded to a significant reduction in the Euler number, whereas the Nusselt number essentially remained unchanged. The longitudinal tube spacing had an insignificant effect on the Nusselt and Euler numbers, and the optimum ratio of the transversal tube spacing to longitudinal tube spacing increased with an increase in the transversal tube spacing. Scaling of the tube spacing had little effect on the Nusselt number but had a significant influence on the Euler number. Finally, predictive correlations for Nusselt and Euler numbers were developed based on the data presented here, and comparisons between the test data from this paper and the predictive values from previously published correlations were performed. ► Tested the thermal–hydraulic characteristics of twelve serrated finned tube banks. ► Presented the effects of the fin density, transversal and longitudinal tube spacing. ► Advanced the correlations of Nusselt and Euler number based on the test data. ► Conducted a comprehensive comparison of the relative correlations in literatures.
doi_str_mv 10.1016/j.applthermaleng.2011.11.037
format article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_1019637704</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S135943111100665X</els_id><sourcerecordid>1019637704</sourcerecordid><originalsourceid>FETCH-LOGICAL-c363t-57096cbadfff7153aa7d3cdb7b2527a01477b81b7fd7f822dc3036e3c4d3bcb33</originalsourceid><addsrcrecordid>eNqNkDtPAzEQhK8AifD4Dy4oaBLs8-WcSDQo4iUh0UBtre114nDxHWsfj3-PUWjokFaaYmdGmq-qzgWfCS7ay-0MhqHLG6QddBjXs5oLMSvHpTqoJkLOl9NGCnFUHae05VzUC9VMKrr5HJDCDmOGjoX4jimHNeTQR9Z7tkHILBPE5JEYRMcGwpRGQuaoH0qAJSSCjI75EGORPBpkBuJrYh8hb1jKsF4jlU8HX_2Y02l16KFLeParJ9XL7c3z6n76-HT3sLp-nFrZyjydK75srQHnvVdiLgGUk9YZZep5rYCLRimzEEZ5p_yirp2VXLYobeOksUbKk-pi3ztQ_zaWXXoXksWug4j9mHTBtmylUrwp1qu91VKfEqHXQ2EC9FVMP75Wb_VfvPoHry5X8Jb47T6OZc57QNLJBowWXSC0Wbs-_K_oGx7Jki0</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1019637704</pqid></control><display><type>article</type><title>Experimental investigation of heat transfer and pressure drop in serrated finned tube banks with staggered layouts</title><source>Elsevier</source><creator>Ma, Youfu ; Yuan, Yichao ; Liu, Yuzheng ; Hu, Xiaohong ; Huang, Yan</creator><creatorcontrib>Ma, Youfu ; Yuan, Yichao ; Liu, Yuzheng ; Hu, Xiaohong ; Huang, Yan</creatorcontrib><description>An experimental study was performed to investigate the heat transfer and pressure drop characteristics of serrated finned tube banks with staggered layouts. The influences of varied fin densities, transversal tube spacing and longitudinal tube spacing were presented. For a constant fin height, an increase in the fin density resulted in an increase in the Euler number, and a gradual decrease in the Nusselt number was observed as the Reynolds number increased. An increase in the transversal tube spacing corresponded to a significant reduction in the Euler number, whereas the Nusselt number essentially remained unchanged. The longitudinal tube spacing had an insignificant effect on the Nusselt and Euler numbers, and the optimum ratio of the transversal tube spacing to longitudinal tube spacing increased with an increase in the transversal tube spacing. Scaling of the tube spacing had little effect on the Nusselt number but had a significant influence on the Euler number. Finally, predictive correlations for Nusselt and Euler numbers were developed based on the data presented here, and comparisons between the test data from this paper and the predictive values from previously published correlations were performed. ► Tested the thermal–hydraulic characteristics of twelve serrated finned tube banks. ► Presented the effects of the fin density, transversal and longitudinal tube spacing. ► Advanced the correlations of Nusselt and Euler number based on the test data. ► Conducted a comprehensive comparison of the relative correlations in literatures.</description><identifier>ISSN: 1359-4311</identifier><identifier>DOI: 10.1016/j.applthermaleng.2011.11.037</identifier><language>eng</language><publisher>Elsevier Ltd</publisher><subject>Banks ; Correlation ; Density ; Finned tube ; Fluid flow ; Heat recovery steam generator ; Heat transfer ; Nusselt number ; Pressure drop ; Serrated fin ; Tubes</subject><ispartof>Applied thermal engineering, 2012-05, Vol.37, p.314-323</ispartof><rights>2011 Elsevier Ltd</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c363t-57096cbadfff7153aa7d3cdb7b2527a01477b81b7fd7f822dc3036e3c4d3bcb33</citedby><cites>FETCH-LOGICAL-c363t-57096cbadfff7153aa7d3cdb7b2527a01477b81b7fd7f822dc3036e3c4d3bcb33</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27922,27923</link.rule.ids></links><search><creatorcontrib>Ma, Youfu</creatorcontrib><creatorcontrib>Yuan, Yichao</creatorcontrib><creatorcontrib>Liu, Yuzheng</creatorcontrib><creatorcontrib>Hu, Xiaohong</creatorcontrib><creatorcontrib>Huang, Yan</creatorcontrib><title>Experimental investigation of heat transfer and pressure drop in serrated finned tube banks with staggered layouts</title><title>Applied thermal engineering</title><description>An experimental study was performed to investigate the heat transfer and pressure drop characteristics of serrated finned tube banks with staggered layouts. The influences of varied fin densities, transversal tube spacing and longitudinal tube spacing were presented. For a constant fin height, an increase in the fin density resulted in an increase in the Euler number, and a gradual decrease in the Nusselt number was observed as the Reynolds number increased. An increase in the transversal tube spacing corresponded to a significant reduction in the Euler number, whereas the Nusselt number essentially remained unchanged. The longitudinal tube spacing had an insignificant effect on the Nusselt and Euler numbers, and the optimum ratio of the transversal tube spacing to longitudinal tube spacing increased with an increase in the transversal tube spacing. Scaling of the tube spacing had little effect on the Nusselt number but had a significant influence on the Euler number. Finally, predictive correlations for Nusselt and Euler numbers were developed based on the data presented here, and comparisons between the test data from this paper and the predictive values from previously published correlations were performed. ► Tested the thermal–hydraulic characteristics of twelve serrated finned tube banks. ► Presented the effects of the fin density, transversal and longitudinal tube spacing. ► Advanced the correlations of Nusselt and Euler number based on the test data. ► Conducted a comprehensive comparison of the relative correlations in literatures.</description><subject>Banks</subject><subject>Correlation</subject><subject>Density</subject><subject>Finned tube</subject><subject>Fluid flow</subject><subject>Heat recovery steam generator</subject><subject>Heat transfer</subject><subject>Nusselt number</subject><subject>Pressure drop</subject><subject>Serrated fin</subject><subject>Tubes</subject><issn>1359-4311</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNqNkDtPAzEQhK8AifD4Dy4oaBLs8-WcSDQo4iUh0UBtre114nDxHWsfj3-PUWjokFaaYmdGmq-qzgWfCS7ay-0MhqHLG6QddBjXs5oLMSvHpTqoJkLOl9NGCnFUHae05VzUC9VMKrr5HJDCDmOGjoX4jimHNeTQR9Z7tkHILBPE5JEYRMcGwpRGQuaoH0qAJSSCjI75EGORPBpkBuJrYh8hb1jKsF4jlU8HX_2Y02l16KFLeParJ9XL7c3z6n76-HT3sLp-nFrZyjydK75srQHnvVdiLgGUk9YZZep5rYCLRimzEEZ5p_yirp2VXLYobeOksUbKk-pi3ztQ_zaWXXoXksWug4j9mHTBtmylUrwp1qu91VKfEqHXQ2EC9FVMP75Wb_VfvPoHry5X8Jb47T6OZc57QNLJBowWXSC0Wbs-_K_oGx7Jki0</recordid><startdate>201205</startdate><enddate>201205</enddate><creator>Ma, Youfu</creator><creator>Yuan, Yichao</creator><creator>Liu, Yuzheng</creator><creator>Hu, Xiaohong</creator><creator>Huang, Yan</creator><general>Elsevier Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>KR7</scope></search><sort><creationdate>201205</creationdate><title>Experimental investigation of heat transfer and pressure drop in serrated finned tube banks with staggered layouts</title><author>Ma, Youfu ; Yuan, Yichao ; Liu, Yuzheng ; Hu, Xiaohong ; Huang, Yan</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c363t-57096cbadfff7153aa7d3cdb7b2527a01477b81b7fd7f822dc3036e3c4d3bcb33</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Banks</topic><topic>Correlation</topic><topic>Density</topic><topic>Finned tube</topic><topic>Fluid flow</topic><topic>Heat recovery steam generator</topic><topic>Heat transfer</topic><topic>Nusselt number</topic><topic>Pressure drop</topic><topic>Serrated fin</topic><topic>Tubes</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ma, Youfu</creatorcontrib><creatorcontrib>Yuan, Yichao</creatorcontrib><creatorcontrib>Liu, Yuzheng</creatorcontrib><creatorcontrib>Hu, Xiaohong</creatorcontrib><creatorcontrib>Huang, Yan</creatorcontrib><collection>CrossRef</collection><collection>Mechanical &amp; Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Applied thermal engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ma, Youfu</au><au>Yuan, Yichao</au><au>Liu, Yuzheng</au><au>Hu, Xiaohong</au><au>Huang, Yan</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Experimental investigation of heat transfer and pressure drop in serrated finned tube banks with staggered layouts</atitle><jtitle>Applied thermal engineering</jtitle><date>2012-05</date><risdate>2012</risdate><volume>37</volume><spage>314</spage><epage>323</epage><pages>314-323</pages><issn>1359-4311</issn><abstract>An experimental study was performed to investigate the heat transfer and pressure drop characteristics of serrated finned tube banks with staggered layouts. The influences of varied fin densities, transversal tube spacing and longitudinal tube spacing were presented. For a constant fin height, an increase in the fin density resulted in an increase in the Euler number, and a gradual decrease in the Nusselt number was observed as the Reynolds number increased. An increase in the transversal tube spacing corresponded to a significant reduction in the Euler number, whereas the Nusselt number essentially remained unchanged. The longitudinal tube spacing had an insignificant effect on the Nusselt and Euler numbers, and the optimum ratio of the transversal tube spacing to longitudinal tube spacing increased with an increase in the transversal tube spacing. Scaling of the tube spacing had little effect on the Nusselt number but had a significant influence on the Euler number. Finally, predictive correlations for Nusselt and Euler numbers were developed based on the data presented here, and comparisons between the test data from this paper and the predictive values from previously published correlations were performed. ► Tested the thermal–hydraulic characteristics of twelve serrated finned tube banks. ► Presented the effects of the fin density, transversal and longitudinal tube spacing. ► Advanced the correlations of Nusselt and Euler number based on the test data. ► Conducted a comprehensive comparison of the relative correlations in literatures.</abstract><pub>Elsevier Ltd</pub><doi>10.1016/j.applthermaleng.2011.11.037</doi><tpages>10</tpages></addata></record>
fulltext fulltext
identifier ISSN: 1359-4311
ispartof Applied thermal engineering, 2012-05, Vol.37, p.314-323
issn 1359-4311
language eng
recordid cdi_proquest_miscellaneous_1019637704
source Elsevier
subjects Banks
Correlation
Density
Finned tube
Fluid flow
Heat recovery steam generator
Heat transfer
Nusselt number
Pressure drop
Serrated fin
Tubes
title Experimental investigation of heat transfer and pressure drop in serrated finned tube banks with staggered layouts
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-14T12%3A36%3A37IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Experimental%20investigation%20of%20heat%20transfer%20and%20pressure%20drop%20in%20serrated%20finned%20tube%20banks%20with%20staggered%20layouts&rft.jtitle=Applied%20thermal%20engineering&rft.au=Ma,%20Youfu&rft.date=2012-05&rft.volume=37&rft.spage=314&rft.epage=323&rft.pages=314-323&rft.issn=1359-4311&rft_id=info:doi/10.1016/j.applthermaleng.2011.11.037&rft_dat=%3Cproquest_cross%3E1019637704%3C/proquest_cross%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c363t-57096cbadfff7153aa7d3cdb7b2527a01477b81b7fd7f822dc3036e3c4d3bcb33%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=1019637704&rft_id=info:pmid/&rfr_iscdi=true