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Visualization experiment of gas–liquid flow pattern downstream of single-orifice plates in horizontal pipes under an intermittent upstream flow
•Flow patterns in DSOP under intermittent upstream flow were identified experimentally.•The effects of JG, JL and β on the flow pattern transition in DSOP were examined.•The flow in DSOP shows stratified and dispersed bubble with intermittent disappeared.•The throttling of orifice plates exhibits ex...
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Published in: | Experimental thermal and fluid science 2020-11, Vol.119, p.110206, Article 110206 |
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description | •Flow patterns in DSOP under intermittent upstream flow were identified experimentally.•The effects of JG, JL and β on the flow pattern transition in DSOP were examined.•The flow in DSOP shows stratified and dispersed bubble with intermittent disappeared.•The throttling of orifice plates exhibits excellent performance on bubble breakup.•A novel criterion is proposed for predicting the stratified/bubble transition in DSOP.
The flow pattern of gas–liquid mixtures across a single-orifice plate in horizontal pipes, in particular the change in flow patterns downstream of a single-orifice plate (DSOP) when the upstream is in a common intermittent flow, has not been elucidated hitherto. In this study, a visualization experiment was performed using air and water as the gas and liquid phases, respectively. The effects of superficial gas velocity, superficial liquid velocity, and orifice-pipe diameter ratio on the flow pattern transition in DSOPs were experimentally examined in ranges of 0.07–0.51 m/s, 0.35–1.77 m/s, and 0.30–0.61, respectively. Results show that there are two different trends, i.e., stratified and dispersed, in DSOPs for an intermittent upstream flow. It is interesting that in DSOPs, intermittent flows tend to disappear, or, stratified flows can transit to bubble flows directly. In DSOPs, most of the region corresponding to an intermittent flow for a simple horizontal pipe becomes the region of a completely dispersed bubble flow, indicating that the throttling of orifice plates has excellent performance on bubble breakup. Moreover, a novel dimensionless criterion is proposed to predict the transition between stratified and bubble flows in DSOPs. |
doi_str_mv | 10.1016/j.expthermflusci.2020.110206 |
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The flow pattern of gas–liquid mixtures across a single-orifice plate in horizontal pipes, in particular the change in flow patterns downstream of a single-orifice plate (DSOP) when the upstream is in a common intermittent flow, has not been elucidated hitherto. In this study, a visualization experiment was performed using air and water as the gas and liquid phases, respectively. The effects of superficial gas velocity, superficial liquid velocity, and orifice-pipe diameter ratio on the flow pattern transition in DSOPs were experimentally examined in ranges of 0.07–0.51 m/s, 0.35–1.77 m/s, and 0.30–0.61, respectively. Results show that there are two different trends, i.e., stratified and dispersed, in DSOPs for an intermittent upstream flow. It is interesting that in DSOPs, intermittent flows tend to disappear, or, stratified flows can transit to bubble flows directly. In DSOPs, most of the region corresponding to an intermittent flow for a simple horizontal pipe becomes the region of a completely dispersed bubble flow, indicating that the throttling of orifice plates has excellent performance on bubble breakup. Moreover, a novel dimensionless criterion is proposed to predict the transition between stratified and bubble flows in DSOPs.</description><identifier>ISSN: 0894-1777</identifier><identifier>EISSN: 1879-2286</identifier><identifier>DOI: 10.1016/j.expthermflusci.2020.110206</identifier><language>eng</language><publisher>Philadelphia: Elsevier Inc</publisher><subject>Bubble ; Bubbles ; Dispersion ; Flow control ; Flow pattern ; Fluid dynamics ; Gas–liquid flow ; Liquid flow ; Liquid phases ; Orifice meters ; Orifice plate ; Orifices ; Pipes ; Stratified flow ; Throttling ; Transition criterion ; Upstream ; Velocity ; Visualization</subject><ispartof>Experimental thermal and fluid science, 2020-11, Vol.119, p.110206, Article 110206</ispartof><rights>2020 Elsevier Inc.</rights><rights>Copyright Elsevier Science Ltd. Nov 1, 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c358t-31782f1fdbd75bc10f5453454ac6d06077ca88a6d94df47308525f3e8157ae73</citedby><cites>FETCH-LOGICAL-c358t-31782f1fdbd75bc10f5453454ac6d06077ca88a6d94df47308525f3e8157ae73</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>Liu, Weiye</creatorcontrib><creatorcontrib>Wu, Hengliang</creatorcontrib><creatorcontrib>Liu, Yuan</creatorcontrib><creatorcontrib>Lyu, Junfu</creatorcontrib><creatorcontrib>Cai, Zhenqi</creatorcontrib><title>Visualization experiment of gas–liquid flow pattern downstream of single-orifice plates in horizontal pipes under an intermittent upstream flow</title><title>Experimental thermal and fluid science</title><description>•Flow patterns in DSOP under intermittent upstream flow were identified experimentally.•The effects of JG, JL and β on the flow pattern transition in DSOP were examined.•The flow in DSOP shows stratified and dispersed bubble with intermittent disappeared.•The throttling of orifice plates exhibits excellent performance on bubble breakup.•A novel criterion is proposed for predicting the stratified/bubble transition in DSOP.
The flow pattern of gas–liquid mixtures across a single-orifice plate in horizontal pipes, in particular the change in flow patterns downstream of a single-orifice plate (DSOP) when the upstream is in a common intermittent flow, has not been elucidated hitherto. In this study, a visualization experiment was performed using air and water as the gas and liquid phases, respectively. The effects of superficial gas velocity, superficial liquid velocity, and orifice-pipe diameter ratio on the flow pattern transition in DSOPs were experimentally examined in ranges of 0.07–0.51 m/s, 0.35–1.77 m/s, and 0.30–0.61, respectively. Results show that there are two different trends, i.e., stratified and dispersed, in DSOPs for an intermittent upstream flow. It is interesting that in DSOPs, intermittent flows tend to disappear, or, stratified flows can transit to bubble flows directly. In DSOPs, most of the region corresponding to an intermittent flow for a simple horizontal pipe becomes the region of a completely dispersed bubble flow, indicating that the throttling of orifice plates has excellent performance on bubble breakup. Moreover, a novel dimensionless criterion is proposed to predict the transition between stratified and bubble flows in DSOPs.</description><subject>Bubble</subject><subject>Bubbles</subject><subject>Dispersion</subject><subject>Flow control</subject><subject>Flow pattern</subject><subject>Fluid dynamics</subject><subject>Gas–liquid flow</subject><subject>Liquid flow</subject><subject>Liquid phases</subject><subject>Orifice meters</subject><subject>Orifice plate</subject><subject>Orifices</subject><subject>Pipes</subject><subject>Stratified flow</subject><subject>Throttling</subject><subject>Transition criterion</subject><subject>Upstream</subject><subject>Velocity</subject><subject>Visualization</subject><issn>0894-1777</issn><issn>1879-2286</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNqNkc9uGyEQxlGUSHH-vANSe10H2GXBUi9VVCeRLOUS5YoIDAnWGjbANq1PeYWqb5gnCZZ96a2XGWnmm98n-BD6SsmcEtpfrefwaywvkDZumLLxc0ZYXdFa-yM0o1IsGsZkf4xmRC66hgohTtFZzmtCiGSUzNCfR58nPfitLj4GXHmQ_AZCwdHhZ50_3v8O_nXyFrshvuFRlwIpYBvfQi4J9Ganyz48D9DE5J03gMdBF8jYB_xSR9sYih7w6Mc6m4KFhHWoy8rZ-EqrVtN4YO08LtCJ00OGy0M_Rw_LHw_Xt83q_ubu-vuqMS2XpWmpkMxRZ5-s4E-GEsc73na806a3pCdCGC2l7u2is64TLZGccdeCpFxoEO05-rLHjim-TpCLWscpheqoWNf1gokF51X1ba8yKeacwKmxfo9OvxUlapeBWqt_M1C7DNQ-g3q-3J9DfchPD0lVBQQD1icwRdno_w_0CcWbnho</recordid><startdate>20201101</startdate><enddate>20201101</enddate><creator>Ma, Youfu</creator><creator>Liu, Weiye</creator><creator>Wu, Hengliang</creator><creator>Liu, Yuan</creator><creator>Lyu, Junfu</creator><creator>Cai, Zhenqi</creator><general>Elsevier Inc</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7TB</scope><scope>7U5</scope><scope>7UA</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>20201101</creationdate><title>Visualization experiment of gas–liquid flow pattern downstream of single-orifice plates in horizontal pipes under an intermittent upstream flow</title><author>Ma, Youfu ; Liu, Weiye ; Wu, Hengliang ; Liu, Yuan ; Lyu, Junfu ; Cai, Zhenqi</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c358t-31782f1fdbd75bc10f5453454ac6d06077ca88a6d94df47308525f3e8157ae73</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Bubble</topic><topic>Bubbles</topic><topic>Dispersion</topic><topic>Flow control</topic><topic>Flow pattern</topic><topic>Fluid dynamics</topic><topic>Gas–liquid flow</topic><topic>Liquid flow</topic><topic>Liquid phases</topic><topic>Orifice meters</topic><topic>Orifice plate</topic><topic>Orifices</topic><topic>Pipes</topic><topic>Stratified flow</topic><topic>Throttling</topic><topic>Transition criterion</topic><topic>Upstream</topic><topic>Velocity</topic><topic>Visualization</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ma, Youfu</creatorcontrib><creatorcontrib>Liu, Weiye</creatorcontrib><creatorcontrib>Wu, Hengliang</creatorcontrib><creatorcontrib>Liu, Yuan</creatorcontrib><creatorcontrib>Lyu, Junfu</creatorcontrib><creatorcontrib>Cai, Zhenqi</creatorcontrib><collection>CrossRef</collection><collection>Aqualine</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Water Resources Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Experimental thermal and fluid science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ma, Youfu</au><au>Liu, Weiye</au><au>Wu, Hengliang</au><au>Liu, Yuan</au><au>Lyu, Junfu</au><au>Cai, Zhenqi</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Visualization experiment of gas–liquid flow pattern downstream of single-orifice plates in horizontal pipes under an intermittent upstream flow</atitle><jtitle>Experimental thermal and fluid science</jtitle><date>2020-11-01</date><risdate>2020</risdate><volume>119</volume><spage>110206</spage><pages>110206-</pages><artnum>110206</artnum><issn>0894-1777</issn><eissn>1879-2286</eissn><abstract>•Flow patterns in DSOP under intermittent upstream flow were identified experimentally.•The effects of JG, JL and β on the flow pattern transition in DSOP were examined.•The flow in DSOP shows stratified and dispersed bubble with intermittent disappeared.•The throttling of orifice plates exhibits excellent performance on bubble breakup.•A novel criterion is proposed for predicting the stratified/bubble transition in DSOP.
The flow pattern of gas–liquid mixtures across a single-orifice plate in horizontal pipes, in particular the change in flow patterns downstream of a single-orifice plate (DSOP) when the upstream is in a common intermittent flow, has not been elucidated hitherto. In this study, a visualization experiment was performed using air and water as the gas and liquid phases, respectively. The effects of superficial gas velocity, superficial liquid velocity, and orifice-pipe diameter ratio on the flow pattern transition in DSOPs were experimentally examined in ranges of 0.07–0.51 m/s, 0.35–1.77 m/s, and 0.30–0.61, respectively. Results show that there are two different trends, i.e., stratified and dispersed, in DSOPs for an intermittent upstream flow. It is interesting that in DSOPs, intermittent flows tend to disappear, or, stratified flows can transit to bubble flows directly. In DSOPs, most of the region corresponding to an intermittent flow for a simple horizontal pipe becomes the region of a completely dispersed bubble flow, indicating that the throttling of orifice plates has excellent performance on bubble breakup. Moreover, a novel dimensionless criterion is proposed to predict the transition between stratified and bubble flows in DSOPs.</abstract><cop>Philadelphia</cop><pub>Elsevier Inc</pub><doi>10.1016/j.expthermflusci.2020.110206</doi></addata></record> |
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subjects | Bubble Bubbles Dispersion Flow control Flow pattern Fluid dynamics Gas–liquid flow Liquid flow Liquid phases Orifice meters Orifice plate Orifices Pipes Stratified flow Throttling Transition criterion Upstream Velocity Visualization |
title | Visualization experiment of gas–liquid flow pattern downstream of single-orifice plates in horizontal pipes under an intermittent upstream flow |
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