Inclination effects on circumferential film flow distribution in annular gas/liquid flows
Measurements of the circumferentially resolved axial liquid film flow rate have been obtained for a 38 mm internal dia. pipe at inclinations of 0°, 20°, 45°, 70 and 85° from the horizontal. The method employed is based on that used by Butterworth, and consists of a film extraction technique which ut...
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Veröffentlicht in: | AIChE journal 2007-05, Vol.53 (5), p.1144-1150 |
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description | Measurements of the circumferentially resolved axial liquid film flow rate have been obtained for a 38 mm internal dia. pipe at inclinations of 0°, 20°, 45°, 70 and 85° from the horizontal. The method employed is based on that used by Butterworth, and consists of a film extraction technique which utilizes a unit with a wall that is porous over a sector of the pipe. Liquid entrained fraction was determined from the total film flow rate. Results show that the local liquid film flow rate is not symmetrical. Flow rates are higher on the lower part of the pipe. As the inclination angle deviates from horizontal, the film flow rate becomes systematically less asymmetric. There is not a strong dependence of the entrained fraction on pipe inclination. For the case when the pipe is horizontal, the circumferential variation of film flow rate is well predicted by a horizontal annular flow model. © 2007 American Institute of Chemical Engineers AIChE J, 2007 |
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For the case when the pipe is horizontal, the circumferential variation of film flow rate is well predicted by a horizontal annular flow model. © 2007 American Institute of Chemical Engineers AIChE J, 2007</description><identifier>ISSN: 0001-1541</identifier><identifier>EISSN: 1547-5905</identifier><identifier>DOI: 10.1002/aic.11155</identifier><identifier>CODEN: AICEAC</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc., A Wiley Company</publisher><subject>annular flow ; Applied sciences ; Chemical engineering ; Effects ; entrained fraction ; Exact sciences and technology ; film flow rate ; Fluid dynamics ; Fluids ; Gas flow ; gas-liquid flow ; Hydrodynamics of contact apparatus ; Measurement ; pipe inclination ; Pipes</subject><ispartof>AIChE journal, 2007-05, Vol.53 (5), p.1144-1150</ispartof><rights>Copyright © 2007 American Institute of Chemical Engineers (AIChE)</rights><rights>2007 INIST-CNRS</rights><rights>Copyright American Institute of Chemical Engineers May 2007</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c5245-7108b168d5dee297226fd7e29d57f90353833710c8cc604a4121b77070d262623</citedby><cites>FETCH-LOGICAL-c5245-7108b168d5dee297226fd7e29d57f90353833710c8cc604a4121b77070d262623</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Faic.11155$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Faic.11155$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,776,780,1411,27903,27904,45553,45554</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=18692089$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Geraci, G.</creatorcontrib><creatorcontrib>Azzopardi, B. J.</creatorcontrib><creatorcontrib>van Maanen, H.R.E.</creatorcontrib><title>Inclination effects on circumferential film flow distribution in annular gas/liquid flows</title><title>AIChE journal</title><addtitle>AIChE J</addtitle><description>Measurements of the circumferentially resolved axial liquid film flow rate have been obtained for a 38 mm internal dia. pipe at inclinations of 0°, 20°, 45°, 70 and 85° from the horizontal. The method employed is based on that used by Butterworth, and consists of a film extraction technique which utilizes a unit with a wall that is porous over a sector of the pipe. Liquid entrained fraction was determined from the total film flow rate. Results show that the local liquid film flow rate is not symmetrical. Flow rates are higher on the lower part of the pipe. As the inclination angle deviates from horizontal, the film flow rate becomes systematically less asymmetric. There is not a strong dependence of the entrained fraction on pipe inclination. For the case when the pipe is horizontal, the circumferential variation of film flow rate is well predicted by a horizontal annular flow model. © 2007 American Institute of Chemical Engineers AIChE J, 2007</description><subject>annular flow</subject><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Effects</subject><subject>entrained fraction</subject><subject>Exact sciences and technology</subject><subject>film flow rate</subject><subject>Fluid dynamics</subject><subject>Fluids</subject><subject>Gas flow</subject><subject>gas-liquid flow</subject><subject>Hydrodynamics of contact apparatus</subject><subject>Measurement</subject><subject>pipe inclination</subject><subject>Pipes</subject><issn>0001-1541</issn><issn>1547-5905</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNqFkV1LHDEUhkOp0K160X8wFFrpxbj5mHxdymrtgiiiIr0K2UxSotmMJjPo_nvjztZCQSUXOefwvC_n8ALwBcF9BCGeam_2EUKUfgATRBteUwnpRzCBEKK6DNAn8Dnnm9JhLvAE_J5HE3zUve9iZZ2zps9VKY1PZlg6m2zsvQ6V82FZudA9VK3PffKLYa3wsdIxDkGn6o_O0-DvB9-uubwDtpwO2e5u_m1w9fPocvarPjk7ns8OTmpDcUNrjqBYICZa2lqLJceYuZaXqqXcSUgoEYQUyAhjGGx0gzBacA45bDErj2yDvdH3LnX3g829WvpsbAg62m7IijeEIFqMC_n9TZKwRjLG0LsglmUpiEUBv_4H3nRDiuVchaQktBkX_DFCJnU5J-vUXfJLnVYKQfUcmiqhqXVohf22MdTZ6OCSjsbnfwLBJIZCFm46cg8-2NXrhupgPvvrXI-KEp99fFHodKsYJ5yq69NjdQ4Fw_z8Qh2SJ6Ovsiw</recordid><startdate>200705</startdate><enddate>200705</enddate><creator>Geraci, G.</creator><creator>Azzopardi, B. 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Flow rates are higher on the lower part of the pipe. As the inclination angle deviates from horizontal, the film flow rate becomes systematically less asymmetric. There is not a strong dependence of the entrained fraction on pipe inclination. For the case when the pipe is horizontal, the circumferential variation of film flow rate is well predicted by a horizontal annular flow model. © 2007 American Institute of Chemical Engineers AIChE J, 2007</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc., A Wiley Company</pub><doi>10.1002/aic.11155</doi><tpages>7</tpages></addata></record> |
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subjects | annular flow Applied sciences Chemical engineering Effects entrained fraction Exact sciences and technology film flow rate Fluid dynamics Fluids Gas flow gas-liquid flow Hydrodynamics of contact apparatus Measurement pipe inclination Pipes |
title | Inclination effects on circumferential film flow distribution in annular gas/liquid flows |
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