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Liquid Film Thickness in Vertical Circular Pipes Under Flooding Conditions at the Top End
In our previous study, we measured the void fraction α, pressure gradient dP/dz, and countercurrent flow limitation in a vertical circular pipe (diameter D = 20 mm) under flooding conditions at the square top end and working fluids of air and water to obtain the wall friction factor f w and the inte...
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Published in: | Nuclear technology 2020-03, Vol.206 (3), p.389-400 |
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creator | Takaki, Toshiya Murase, Michio Nishida, Koji Goda, Raito Shimamura, Takeyuki Tomiyama, Akio |
description | In our previous study, we measured the void fraction α, pressure gradient dP/dz, and countercurrent flow limitation in a vertical circular pipe (diameter D = 20 mm) under flooding conditions at the square top end and working fluids of air and water to obtain the wall friction factor f
w
and the interfacial friction factor f
i
based on the annular flow model. The thickness of the falling liquid film δ obtained from the measured α was relatively well expressed by the correlation for the free-falling film, and the obtained f
w
was well expressed by the Fanning friction factor f for a circular pipe. Measurements of α in vertical pipes under flooding conditions are few. In this study, therefore, we evaluated α and δ from the measured dP/dz under flooding at the square top end reported by Bharathan et al. with D = 50.8 mm and air-water and by Ilyukhin et al. with D = 20 mm and working fluids of steam and water at pressures of P = 0.6 to 4.1 MPa. As a result, we found that δ obtained from the measured dP/dz and the correlation of f
w
= f were well correlated in terms of the liquid Reynolds number Re
L
. The obtained δ was well expressed by the Nusselt's correlation for the free-falling film in the region of laminar flows, but the obtained δ was larger than the Feind's correlation for the free-falling film in the region of turbulent flows due to the interfacial friction. We also discussed effects of the diameter and fluid properties on the interfacial friction factor f
i
. |
doi_str_mv | 10.1080/00295450.2019.1656521 |
format | article |
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w
and the interfacial friction factor f
i
based on the annular flow model. The thickness of the falling liquid film δ obtained from the measured α was relatively well expressed by the correlation for the free-falling film, and the obtained f
w
was well expressed by the Fanning friction factor f for a circular pipe. Measurements of α in vertical pipes under flooding conditions are few. In this study, therefore, we evaluated α and δ from the measured dP/dz under flooding at the square top end reported by Bharathan et al. with D = 50.8 mm and air-water and by Ilyukhin et al. with D = 20 mm and working fluids of steam and water at pressures of P = 0.6 to 4.1 MPa. As a result, we found that δ obtained from the measured dP/dz and the correlation of f
w
= f were well correlated in terms of the liquid Reynolds number Re
L
. The obtained δ was well expressed by the Nusselt's correlation for the free-falling film in the region of laminar flows, but the obtained δ was larger than the Feind's correlation for the free-falling film in the region of turbulent flows due to the interfacial friction. We also discussed effects of the diameter and fluid properties on the interfacial friction factor f
i
.</description><identifier>ISSN: 0029-5450</identifier><identifier>EISSN: 1943-7471</identifier><identifier>DOI: 10.1080/00295450.2019.1656521</identifier><language>eng</language><publisher>La Grange Park: Taylor & Francis</publisher><subject>Countercurrent flow ; flooding ; liquid film thickness ; square top end ; vertical pipe</subject><ispartof>Nuclear technology, 2020-03, Vol.206 (3), p.389-400</ispartof><rights>2019 American Nuclear Society 2019</rights><rights>Copyright American Nuclear Society Mar 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c404t-dd1e9af2ed9c4f88bf27ebfb58cb730806a071fcb7fecfbe8fc2cf48264e2d2d3</citedby><cites>FETCH-LOGICAL-c404t-dd1e9af2ed9c4f88bf27ebfb58cb730806a071fcb7fecfbe8fc2cf48264e2d2d3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Takaki, Toshiya</creatorcontrib><creatorcontrib>Murase, Michio</creatorcontrib><creatorcontrib>Nishida, Koji</creatorcontrib><creatorcontrib>Goda, Raito</creatorcontrib><creatorcontrib>Shimamura, Takeyuki</creatorcontrib><creatorcontrib>Tomiyama, Akio</creatorcontrib><title>Liquid Film Thickness in Vertical Circular Pipes Under Flooding Conditions at the Top End</title><title>Nuclear technology</title><description>In our previous study, we measured the void fraction α, pressure gradient dP/dz, and countercurrent flow limitation in a vertical circular pipe (diameter D = 20 mm) under flooding conditions at the square top end and working fluids of air and water to obtain the wall friction factor f
w
and the interfacial friction factor f
i
based on the annular flow model. The thickness of the falling liquid film δ obtained from the measured α was relatively well expressed by the correlation for the free-falling film, and the obtained f
w
was well expressed by the Fanning friction factor f for a circular pipe. Measurements of α in vertical pipes under flooding conditions are few. In this study, therefore, we evaluated α and δ from the measured dP/dz under flooding at the square top end reported by Bharathan et al. with D = 50.8 mm and air-water and by Ilyukhin et al. with D = 20 mm and working fluids of steam and water at pressures of P = 0.6 to 4.1 MPa. As a result, we found that δ obtained from the measured dP/dz and the correlation of f
w
= f were well correlated in terms of the liquid Reynolds number Re
L
. The obtained δ was well expressed by the Nusselt's correlation for the free-falling film in the region of laminar flows, but the obtained δ was larger than the Feind's correlation for the free-falling film in the region of turbulent flows due to the interfacial friction. We also discussed effects of the diameter and fluid properties on the interfacial friction factor f
i
.</description><subject>Countercurrent flow</subject><subject>flooding</subject><subject>liquid film thickness</subject><subject>square top end</subject><subject>vertical pipe</subject><issn>0029-5450</issn><issn>1943-7471</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9kF1LwzAUhoMoOKc_QQh43ZmkaZPeKcOpMNCLTfAqpPlwmV3SJS2yf2_L5q1XhwPP-x7OA8AtRjOMOLpHiFQFLdCMIFzNcFmUBcFnYIIrmmeMMnwOJiOTjdAluEppO6yMIToBn0u3752GC9fs4Grj1Lc3KUHn4YeJnVOygXMXVd_ICN9daxJce20iXDQhaOe_4Dx47ToXfIKyg93GwFVo4ZPX1-DCyiaZm9OcgvXiaTV_yZZvz6_zx2WmKKJdpjU2lbTE6EpRy3ltCTO1rQuuapYP75USMWyHxRpla8OtIspSTkpqiCY6n4K7Y28bw743qRPb0Ec_nBQkZ1WJCOF8oIojpWJIKRor2uh2Mh4ERmK0KP4sitGiOFkccg_HnPM2xJ38CbHRopOHJkQbpVcuifz_il8ec3nd</recordid><startdate>20200303</startdate><enddate>20200303</enddate><creator>Takaki, Toshiya</creator><creator>Murase, Michio</creator><creator>Nishida, Koji</creator><creator>Goda, Raito</creator><creator>Shimamura, Takeyuki</creator><creator>Tomiyama, Akio</creator><general>Taylor & Francis</general><general>American Nuclear Society</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20200303</creationdate><title>Liquid Film Thickness in Vertical Circular Pipes Under Flooding Conditions at the Top End</title><author>Takaki, Toshiya ; Murase, Michio ; Nishida, Koji ; Goda, Raito ; Shimamura, Takeyuki ; Tomiyama, Akio</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c404t-dd1e9af2ed9c4f88bf27ebfb58cb730806a071fcb7fecfbe8fc2cf48264e2d2d3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Countercurrent flow</topic><topic>flooding</topic><topic>liquid film thickness</topic><topic>square top end</topic><topic>vertical pipe</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Takaki, Toshiya</creatorcontrib><creatorcontrib>Murase, Michio</creatorcontrib><creatorcontrib>Nishida, Koji</creatorcontrib><creatorcontrib>Goda, Raito</creatorcontrib><creatorcontrib>Shimamura, Takeyuki</creatorcontrib><creatorcontrib>Tomiyama, Akio</creatorcontrib><collection>CrossRef</collection><jtitle>Nuclear technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Takaki, Toshiya</au><au>Murase, Michio</au><au>Nishida, Koji</au><au>Goda, Raito</au><au>Shimamura, Takeyuki</au><au>Tomiyama, Akio</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Liquid Film Thickness in Vertical Circular Pipes Under Flooding Conditions at the Top End</atitle><jtitle>Nuclear technology</jtitle><date>2020-03-03</date><risdate>2020</risdate><volume>206</volume><issue>3</issue><spage>389</spage><epage>400</epage><pages>389-400</pages><issn>0029-5450</issn><eissn>1943-7471</eissn><abstract>In our previous study, we measured the void fraction α, pressure gradient dP/dz, and countercurrent flow limitation in a vertical circular pipe (diameter D = 20 mm) under flooding conditions at the square top end and working fluids of air and water to obtain the wall friction factor f
w
and the interfacial friction factor f
i
based on the annular flow model. The thickness of the falling liquid film δ obtained from the measured α was relatively well expressed by the correlation for the free-falling film, and the obtained f
w
was well expressed by the Fanning friction factor f for a circular pipe. Measurements of α in vertical pipes under flooding conditions are few. In this study, therefore, we evaluated α and δ from the measured dP/dz under flooding at the square top end reported by Bharathan et al. with D = 50.8 mm and air-water and by Ilyukhin et al. with D = 20 mm and working fluids of steam and water at pressures of P = 0.6 to 4.1 MPa. As a result, we found that δ obtained from the measured dP/dz and the correlation of f
w
= f were well correlated in terms of the liquid Reynolds number Re
L
. The obtained δ was well expressed by the Nusselt's correlation for the free-falling film in the region of laminar flows, but the obtained δ was larger than the Feind's correlation for the free-falling film in the region of turbulent flows due to the interfacial friction. We also discussed effects of the diameter and fluid properties on the interfacial friction factor f
i
.</abstract><cop>La Grange Park</cop><pub>Taylor & Francis</pub><doi>10.1080/00295450.2019.1656521</doi><tpages>12</tpages></addata></record> |
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subjects | Countercurrent flow flooding liquid film thickness square top end vertical pipe |
title | Liquid Film Thickness in Vertical Circular Pipes Under Flooding Conditions at the Top End |
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