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Experimental Investigations and Numerical Assessment of Liquid Velocity Profiles and Turbulence for Single- and Two-phase Flow in a Constricted Vertical Pipe
•The performance of different turbulence models is presented for 3D flow conditions.•For comparison, simulations are performed for both single- and two-phase flows.•Experiments with a combination of HFA and UFXCT are performed for validation.•The liquid velocity and turbulent kinetic energy are anal...
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Published in: | International journal of multiphase flow 2022-12, Vol.157, p.104224, Article 104224 |
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container_title | International journal of multiphase flow |
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creator | Tas-Koehler, Sibel Neumann-Kipping, Martin Liao, Yixiang Bieberle, André Hampel, Uwe |
description | •The performance of different turbulence models is presented for 3D flow conditions.•For comparison, simulations are performed for both single- and two-phase flows.•Experiments with a combination of HFA and UFXCT are performed for validation.•The liquid velocity and turbulent kinetic energy are analyzed.
In this work, the capabilities of state-of-the-art turbulence models are compared for a three-dimensional flow (3D) field within a constricted vertical pipe. The considered flow domain is a vertical pipe section with a baffle-shaped flow constriction which leads to the development of a jet flow through and a recirculation flow region behind the constriction. Different Reynolds-Averaged Navier-Stokes (RANS) and Large Eddy Simulation (LES) models were tested for single- and two-phase flow simulations. In the two-phase simulations, bubble-induced turbulence (BIT) was also considered by adding source terms in the k and ε/ω equations. The results are validated against experimental data. We employed hot-film anemometry (HFA) for liquid velocity measurement and combined it with ultrafast X-ray computed tomography (UFXCT), which provides gas phase data. Based on the local phase-indicator function obtained from the tomographic image data, we can correct HFA signals, which become corrupted by bubble contacts. We found that for single-phase flow all RANS models predict axial velocity well while radial velocity prediction is inadequate. LES models, however, achieve a better prediction of the latter. For two-phase flow, the axial component of the liquid velocity is well captured by all RANS models and the radial component of the liquid velocity is predicted better than for single-phase flow. In general, the computationally less costly RNG k-ε model performs similar to the SSG RSM model and can therefore be recommended for simulation of complex flow scenarios. |
doi_str_mv | 10.1016/j.ijmultiphaseflow.2022.104224 |
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In this work, the capabilities of state-of-the-art turbulence models are compared for a three-dimensional flow (3D) field within a constricted vertical pipe. The considered flow domain is a vertical pipe section with a baffle-shaped flow constriction which leads to the development of a jet flow through and a recirculation flow region behind the constriction. Different Reynolds-Averaged Navier-Stokes (RANS) and Large Eddy Simulation (LES) models were tested for single- and two-phase flow simulations. In the two-phase simulations, bubble-induced turbulence (BIT) was also considered by adding source terms in the k and ε/ω equations. The results are validated against experimental data. We employed hot-film anemometry (HFA) for liquid velocity measurement and combined it with ultrafast X-ray computed tomography (UFXCT), which provides gas phase data. Based on the local phase-indicator function obtained from the tomographic image data, we can correct HFA signals, which become corrupted by bubble contacts. We found that for single-phase flow all RANS models predict axial velocity well while radial velocity prediction is inadequate. LES models, however, achieve a better prediction of the latter. For two-phase flow, the axial component of the liquid velocity is well captured by all RANS models and the radial component of the liquid velocity is predicted better than for single-phase flow. In general, the computationally less costly RNG k-ε model performs similar to the SSG RSM model and can therefore be recommended for simulation of complex flow scenarios.</description><identifier>ISSN: 0301-9322</identifier><identifier>EISSN: 1879-3533</identifier><identifier>DOI: 10.1016/j.ijmultiphaseflow.2022.104224</identifier><language>eng</language><publisher>Elsevier Ltd</publisher><subject>Bubbly two-phase flow ; CFD modelling ; Computed tomography ; Hot-film anemometry ; Liquid velocity ; Turbulent kinetic energy</subject><ispartof>International journal of multiphase flow, 2022-12, Vol.157, p.104224, Article 104224</ispartof><rights>2022</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c266t-9e736e4407e7cb0b722bf277cae7010f394d3ce3a7b92ffec295b8374706e1063</citedby><cites>FETCH-LOGICAL-c266t-9e736e4407e7cb0b722bf277cae7010f394d3ce3a7b92ffec295b8374706e1063</cites><orcidid>0000-0001-9264-5129</orcidid></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>Tas-Koehler, Sibel</creatorcontrib><creatorcontrib>Neumann-Kipping, Martin</creatorcontrib><creatorcontrib>Liao, Yixiang</creatorcontrib><creatorcontrib>Bieberle, André</creatorcontrib><creatorcontrib>Hampel, Uwe</creatorcontrib><title>Experimental Investigations and Numerical Assessment of Liquid Velocity Profiles and Turbulence for Single- and Two-phase Flow in a Constricted Vertical Pipe</title><title>International journal of multiphase flow</title><description>•The performance of different turbulence models is presented for 3D flow conditions.•For comparison, simulations are performed for both single- and two-phase flows.•Experiments with a combination of HFA and UFXCT are performed for validation.•The liquid velocity and turbulent kinetic energy are analyzed.
In this work, the capabilities of state-of-the-art turbulence models are compared for a three-dimensional flow (3D) field within a constricted vertical pipe. The considered flow domain is a vertical pipe section with a baffle-shaped flow constriction which leads to the development of a jet flow through and a recirculation flow region behind the constriction. Different Reynolds-Averaged Navier-Stokes (RANS) and Large Eddy Simulation (LES) models were tested for single- and two-phase flow simulations. In the two-phase simulations, bubble-induced turbulence (BIT) was also considered by adding source terms in the k and ε/ω equations. The results are validated against experimental data. We employed hot-film anemometry (HFA) for liquid velocity measurement and combined it with ultrafast X-ray computed tomography (UFXCT), which provides gas phase data. Based on the local phase-indicator function obtained from the tomographic image data, we can correct HFA signals, which become corrupted by bubble contacts. We found that for single-phase flow all RANS models predict axial velocity well while radial velocity prediction is inadequate. LES models, however, achieve a better prediction of the latter. For two-phase flow, the axial component of the liquid velocity is well captured by all RANS models and the radial component of the liquid velocity is predicted better than for single-phase flow. In general, the computationally less costly RNG k-ε model performs similar to the SSG RSM model and can therefore be recommended for simulation of complex flow scenarios.</description><subject>Bubbly two-phase flow</subject><subject>CFD modelling</subject><subject>Computed tomography</subject><subject>Hot-film anemometry</subject><subject>Liquid velocity</subject><subject>Turbulent kinetic energy</subject><issn>0301-9322</issn><issn>1879-3533</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2022</creationdate><recordtype>article</recordtype><recordid>eNqNkE9PwyAchonRxPnnO3Dy1kmhK-vFZFnUmSy6xOmVUPpDabpSgU79MH5XqfXkyROHF5735UHoIiXTlKT5ZT019a5vgulepQfd2PcpJZTGMKM0O0CTdM6LhM0YO0QTwkiaFIzSY3TifU0ImfGMTdDX9UcHzuygDbLBd-0efDAvMhjbeizbCt_3u5irGC68B--Hm9hqvDZvvanwMzRWmfCJN85q08D4aNu7sm-gVYC1dfjRtC8NJGP0bpOfwfgmLsamxRIvY1mIJQEGoAs_dRvTwRk60rLxcP57nqKnm-vtcpWsH27vlot1omieh6QAznLIMsKBq5KUnNJSU86VBE5SolmRVUwBk7wsqNagaDEr54xnnOSQkpydoquRq5z13oEWXXQi3adIiRhki1r8lS0G2WKUHQGrEQBx5d6AE16Z4f-VcaCCqKz5L-obDGKWpg</recordid><startdate>202212</startdate><enddate>202212</enddate><creator>Tas-Koehler, Sibel</creator><creator>Neumann-Kipping, Martin</creator><creator>Liao, Yixiang</creator><creator>Bieberle, André</creator><creator>Hampel, Uwe</creator><general>Elsevier Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0001-9264-5129</orcidid></search><sort><creationdate>202212</creationdate><title>Experimental Investigations and Numerical Assessment of Liquid Velocity Profiles and Turbulence for Single- and Two-phase Flow in a Constricted Vertical Pipe</title><author>Tas-Koehler, Sibel ; Neumann-Kipping, Martin ; Liao, Yixiang ; Bieberle, André ; Hampel, Uwe</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c266t-9e736e4407e7cb0b722bf277cae7010f394d3ce3a7b92ffec295b8374706e1063</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2022</creationdate><topic>Bubbly two-phase flow</topic><topic>CFD modelling</topic><topic>Computed tomography</topic><topic>Hot-film anemometry</topic><topic>Liquid velocity</topic><topic>Turbulent kinetic energy</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Tas-Koehler, Sibel</creatorcontrib><creatorcontrib>Neumann-Kipping, Martin</creatorcontrib><creatorcontrib>Liao, Yixiang</creatorcontrib><creatorcontrib>Bieberle, André</creatorcontrib><creatorcontrib>Hampel, Uwe</creatorcontrib><collection>CrossRef</collection><jtitle>International journal of multiphase flow</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Tas-Koehler, Sibel</au><au>Neumann-Kipping, Martin</au><au>Liao, Yixiang</au><au>Bieberle, André</au><au>Hampel, Uwe</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Experimental Investigations and Numerical Assessment of Liquid Velocity Profiles and Turbulence for Single- and Two-phase Flow in a Constricted Vertical Pipe</atitle><jtitle>International journal of multiphase flow</jtitle><date>2022-12</date><risdate>2022</risdate><volume>157</volume><spage>104224</spage><pages>104224-</pages><artnum>104224</artnum><issn>0301-9322</issn><eissn>1879-3533</eissn><abstract>•The performance of different turbulence models is presented for 3D flow conditions.•For comparison, simulations are performed for both single- and two-phase flows.•Experiments with a combination of HFA and UFXCT are performed for validation.•The liquid velocity and turbulent kinetic energy are analyzed.
In this work, the capabilities of state-of-the-art turbulence models are compared for a three-dimensional flow (3D) field within a constricted vertical pipe. The considered flow domain is a vertical pipe section with a baffle-shaped flow constriction which leads to the development of a jet flow through and a recirculation flow region behind the constriction. Different Reynolds-Averaged Navier-Stokes (RANS) and Large Eddy Simulation (LES) models were tested for single- and two-phase flow simulations. In the two-phase simulations, bubble-induced turbulence (BIT) was also considered by adding source terms in the k and ε/ω equations. The results are validated against experimental data. We employed hot-film anemometry (HFA) for liquid velocity measurement and combined it with ultrafast X-ray computed tomography (UFXCT), which provides gas phase data. Based on the local phase-indicator function obtained from the tomographic image data, we can correct HFA signals, which become corrupted by bubble contacts. We found that for single-phase flow all RANS models predict axial velocity well while radial velocity prediction is inadequate. LES models, however, achieve a better prediction of the latter. For two-phase flow, the axial component of the liquid velocity is well captured by all RANS models and the radial component of the liquid velocity is predicted better than for single-phase flow. In general, the computationally less costly RNG k-ε model performs similar to the SSG RSM model and can therefore be recommended for simulation of complex flow scenarios.</abstract><pub>Elsevier Ltd</pub><doi>10.1016/j.ijmultiphaseflow.2022.104224</doi><orcidid>https://orcid.org/0000-0001-9264-5129</orcidid></addata></record> |
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subjects | Bubbly two-phase flow CFD modelling Computed tomography Hot-film anemometry Liquid velocity Turbulent kinetic energy |
title | Experimental Investigations and Numerical Assessment of Liquid Velocity Profiles and Turbulence for Single- and Two-phase Flow in a Constricted Vertical Pipe |
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