Particle removal from a surface by a bounded vortex flow
A bounded vortex flow consists of an axisymmetric vortex that is confined top and bottom between two plates (the “confinement plate” and “impingement plate”, respectively) and surrounded laterally by a swirling annular slot jet. The bottom of the vortex terminates on the boundary layer along the imp...
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description | A bounded vortex flow consists of an axisymmetric vortex that is confined top and bottom between two plates (the “confinement plate” and “impingement plate”, respectively) and surrounded laterally by a swirling annular slot jet. The bottom of the vortex terminates on the boundary layer along the impingement plate and the top of the vortex is drawn into a suction port positioned at the center of the confinement plate. The circumferential flow within the annular jet is important for supplying circulation to the central wall-normal vortex. This flow field is proposed as a method for mitigation of dust build-up on a surface, where the vortex–jet combination supplements the more traditional vacuum port by enhancing the surface shear stress and related particle transport rate. The paper reports on a computational study of the velocity field and particle transport by a bounded vortex flow. Fluid flow computations are performed using a finite-volume approach for an incompressible fluid and particle transport is simulated using a discrete-element method. Computations are performed for different values of two dimensionless parameters – the ratio of the plate separation distance and the average radial location of the jet inlet (the dimensionless
confinement height) and the ratio of flow rate withdrawn at the suction outlet and that injected by the jet (the
flow rate ratio). For small values of the flow rate ratio, the impinging jet streamlines pass down to the boundary layer along the bottom surface and then travel up the vortex core. By contrast, for large values of flow rate ratio, the annular jet is quickly entrained into the suction outlet and no wall-normal vortex is formed. Particles are observed to roll along the impingement surface in a direction determined by the fluid shear stress lines. Particles roll outward when they lie beyond a separatrix curve of the surface shear stress lines, where particles within this separatrix curve roll inward, piling up at the center of the flow field. A toroidal vortex ring forms for the small confinement height case with flow rate ratio equal to unity, which yields double separatrix curves in the shear stress lines. The inward rolling particles intermittently lift up due to collision forces and burst away from the impingement surface, eventually to become entrained into the flow out the suction port or resettling back onto the impingement surface. |
doi_str_mv | 10.1016/j.ijheatfluidflow.2011.07.003 |
format | Article |
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confinement height) and the ratio of flow rate withdrawn at the suction outlet and that injected by the jet (the
flow rate ratio). For small values of the flow rate ratio, the impinging jet streamlines pass down to the boundary layer along the bottom surface and then travel up the vortex core. By contrast, for large values of flow rate ratio, the annular jet is quickly entrained into the suction outlet and no wall-normal vortex is formed. Particles are observed to roll along the impingement surface in a direction determined by the fluid shear stress lines. Particles roll outward when they lie beyond a separatrix curve of the surface shear stress lines, where particles within this separatrix curve roll inward, piling up at the center of the flow field. A toroidal vortex ring forms for the small confinement height case with flow rate ratio equal to unity, which yields double separatrix curves in the shear stress lines. The inward rolling particles intermittently lift up due to collision forces and burst away from the impingement surface, eventually to become entrained into the flow out the suction port or resettling back onto the impingement surface.</description><identifier>ISSN: 0142-727X</identifier><identifier>EISSN: 1879-2278</identifier><identifier>DOI: 10.1016/j.ijheatfluidflow.2011.07.003</identifier><identifier>CODEN: IJHFD2</identifier><language>eng</language><publisher>New York, NY: Elsevier Inc</publisher><subject>Applied sciences ; Centrifugation, cyclones ; Chemical engineering ; Computational fluid dynamics ; Confinement ; Exact sciences and technology ; Flow rate ; Fluid flow ; Impingement ; Jet impingement ; Liquid-liquid and fluid-solid mechanical separations ; Particle entrainment ; Plates ; Shear stress ; Vortex–wall interaction ; Vortices</subject><ispartof>The International journal of heat and fluid flow, 2011-10, Vol.32 (5), p.901-914</ispartof><rights>2011 Elsevier Inc.</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c395t-ddd9fe4cf4fc7dc1b79e920cab92ef44c3991eac2136b075355cc1ad445f33123</citedby><cites>FETCH-LOGICAL-c395t-ddd9fe4cf4fc7dc1b79e920cab92ef44c3991eac2136b075355cc1ad445f33123</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0142727X11001032$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3536,27903,27904,65309</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=24544488$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Maynard, A.B.</creatorcontrib><creatorcontrib>Marshall, J.S.</creatorcontrib><title>Particle removal from a surface by a bounded vortex flow</title><title>The International journal of heat and fluid flow</title><description>A bounded vortex flow consists of an axisymmetric vortex that is confined top and bottom between two plates (the “confinement plate” and “impingement plate”, respectively) and surrounded laterally by a swirling annular slot jet. The bottom of the vortex terminates on the boundary layer along the impingement plate and the top of the vortex is drawn into a suction port positioned at the center of the confinement plate. The circumferential flow within the annular jet is important for supplying circulation to the central wall-normal vortex. This flow field is proposed as a method for mitigation of dust build-up on a surface, where the vortex–jet combination supplements the more traditional vacuum port by enhancing the surface shear stress and related particle transport rate. The paper reports on a computational study of the velocity field and particle transport by a bounded vortex flow. Fluid flow computations are performed using a finite-volume approach for an incompressible fluid and particle transport is simulated using a discrete-element method. Computations are performed for different values of two dimensionless parameters – the ratio of the plate separation distance and the average radial location of the jet inlet (the dimensionless
confinement height) and the ratio of flow rate withdrawn at the suction outlet and that injected by the jet (the
flow rate ratio). For small values of the flow rate ratio, the impinging jet streamlines pass down to the boundary layer along the bottom surface and then travel up the vortex core. By contrast, for large values of flow rate ratio, the annular jet is quickly entrained into the suction outlet and no wall-normal vortex is formed. Particles are observed to roll along the impingement surface in a direction determined by the fluid shear stress lines. Particles roll outward when they lie beyond a separatrix curve of the surface shear stress lines, where particles within this separatrix curve roll inward, piling up at the center of the flow field. A toroidal vortex ring forms for the small confinement height case with flow rate ratio equal to unity, which yields double separatrix curves in the shear stress lines. The inward rolling particles intermittently lift up due to collision forces and burst away from the impingement surface, eventually to become entrained into the flow out the suction port or resettling back onto the impingement surface.</description><subject>Applied sciences</subject><subject>Centrifugation, cyclones</subject><subject>Chemical engineering</subject><subject>Computational fluid dynamics</subject><subject>Confinement</subject><subject>Exact sciences and technology</subject><subject>Flow rate</subject><subject>Fluid flow</subject><subject>Impingement</subject><subject>Jet impingement</subject><subject>Liquid-liquid and fluid-solid mechanical separations</subject><subject>Particle entrainment</subject><subject>Plates</subject><subject>Shear stress</subject><subject>Vortex–wall interaction</subject><subject>Vortices</subject><issn>0142-727X</issn><issn>1879-2278</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><recordid>eNqNkMFKAzEQhoMoWKvvsJfiadckm202Bw9StAoFPSh4C9nJBFO2TU12q317t7R48ORpGPjm_5mPkAmjBaNserMs_PIDTefa3lvXhq-CU8YKKgtKyxMyYrVUOeeyPiUjygTPJZfv5-QipSWldEqFHJH6xcTOQ4tZxFXYmjZzMawyk6U-OgOYNbthaUK_tmizbYgdfmf7rkty5kyb8Oo4x-Tt4f519pgvnudPs7tFDqWqutxaqxwKcMKBtMAaqVBxCqZRHJ0QA6UYGuCsnDZUVmVVATBjhahcWTJejsn1IXcTw2ePqdMrnwDb1qwx9EkrplTJlJADeXsgIYaUIjq9iX5l4k4zqvfC9FL_Eab3wjSVehA23E-OTSaBaV00a_DpN4SLSghR1wM3P3A4vL31GHUCj2tA6yNCp23w_2z8ATCgizE</recordid><startdate>20111001</startdate><enddate>20111001</enddate><creator>Maynard, A.B.</creator><creator>Marshall, J.S.</creator><general>Elsevier Inc</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>7U5</scope><scope>8FD</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>20111001</creationdate><title>Particle removal from a surface by a bounded vortex flow</title><author>Maynard, A.B. ; Marshall, J.S.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c395t-ddd9fe4cf4fc7dc1b79e920cab92ef44c3991eac2136b075355cc1ad445f33123</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>Applied sciences</topic><topic>Centrifugation, cyclones</topic><topic>Chemical engineering</topic><topic>Computational fluid dynamics</topic><topic>Confinement</topic><topic>Exact sciences and technology</topic><topic>Flow rate</topic><topic>Fluid flow</topic><topic>Impingement</topic><topic>Jet impingement</topic><topic>Liquid-liquid and fluid-solid mechanical separations</topic><topic>Particle entrainment</topic><topic>Plates</topic><topic>Shear stress</topic><topic>Vortex–wall interaction</topic><topic>Vortices</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Maynard, A.B.</creatorcontrib><creatorcontrib>Marshall, J.S.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>The International journal of heat and fluid flow</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Maynard, A.B.</au><au>Marshall, J.S.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Particle removal from a surface by a bounded vortex flow</atitle><jtitle>The International journal of heat and fluid flow</jtitle><date>2011-10-01</date><risdate>2011</risdate><volume>32</volume><issue>5</issue><spage>901</spage><epage>914</epage><pages>901-914</pages><issn>0142-727X</issn><eissn>1879-2278</eissn><coden>IJHFD2</coden><abstract>A bounded vortex flow consists of an axisymmetric vortex that is confined top and bottom between two plates (the “confinement plate” and “impingement plate”, respectively) and surrounded laterally by a swirling annular slot jet. The bottom of the vortex terminates on the boundary layer along the impingement plate and the top of the vortex is drawn into a suction port positioned at the center of the confinement plate. The circumferential flow within the annular jet is important for supplying circulation to the central wall-normal vortex. This flow field is proposed as a method for mitigation of dust build-up on a surface, where the vortex–jet combination supplements the more traditional vacuum port by enhancing the surface shear stress and related particle transport rate. The paper reports on a computational study of the velocity field and particle transport by a bounded vortex flow. Fluid flow computations are performed using a finite-volume approach for an incompressible fluid and particle transport is simulated using a discrete-element method. Computations are performed for different values of two dimensionless parameters – the ratio of the plate separation distance and the average radial location of the jet inlet (the dimensionless
confinement height) and the ratio of flow rate withdrawn at the suction outlet and that injected by the jet (the
flow rate ratio). For small values of the flow rate ratio, the impinging jet streamlines pass down to the boundary layer along the bottom surface and then travel up the vortex core. By contrast, for large values of flow rate ratio, the annular jet is quickly entrained into the suction outlet and no wall-normal vortex is formed. Particles are observed to roll along the impingement surface in a direction determined by the fluid shear stress lines. Particles roll outward when they lie beyond a separatrix curve of the surface shear stress lines, where particles within this separatrix curve roll inward, piling up at the center of the flow field. A toroidal vortex ring forms for the small confinement height case with flow rate ratio equal to unity, which yields double separatrix curves in the shear stress lines. The inward rolling particles intermittently lift up due to collision forces and burst away from the impingement surface, eventually to become entrained into the flow out the suction port or resettling back onto the impingement surface.</abstract><cop>New York, NY</cop><pub>Elsevier Inc</pub><doi>10.1016/j.ijheatfluidflow.2011.07.003</doi><tpages>14</tpages></addata></record> |
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subjects | Applied sciences Centrifugation, cyclones Chemical engineering Computational fluid dynamics Confinement Exact sciences and technology Flow rate Fluid flow Impingement Jet impingement Liquid-liquid and fluid-solid mechanical separations Particle entrainment Plates Shear stress Vortex–wall interaction Vortices |
title | Particle removal from a surface by a bounded vortex flow |
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