On a eulerian and lagrangian combined model in dense particle-laden riser flow
A new numerical model using both Eulerian and Lagrangian coordinates, and taking account of interparticle interactions, has been developed for the study of hydrodynamic aspects of dense particle‐laden rise flows. A stochastic particle dispersion model has been incorporated in the original model to d...
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Veröffentlicht in: | Canadian journal of chemical engineering 1999-12, Vol.77 (6), p.1113-1120 |
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creator | Fan, Jianren Sun, Ping Ma, Yinliang Cen, Kefa |
description | A new numerical model using both Eulerian and Lagrangian coordinates, and taking account of interparticle interactions, has been developed for the study of hydrodynamic aspects of dense particle‐laden rise flows. A stochastic particle dispersion model has been incorporated in the original model to describe the gas particle turbulent flows. In addition, the collisional interaction between the particles has been modeled using the kinetic theory of granular flows based on the Chapman‐Enskog theory of dense gases. A comparison with the experimental results of Miller and Gidspow (1992) shows reasonably good agreement. The present model may provide a useful approach for predicting the complex hydrodynamic behaviour of fluidized bed systems.
Un nouveau modèle numérique utilisant à la fois des coordonnées eulériennes et lagrangiennes et tenant compte desinteractions entre les particules a été mis au point pour l'étude des aspects hydrodynamiques d'écoulements ascendants chargés de particules denses. Un modèle de dispersion de particules stochastique est introduit au modèle original afin de décrire les écoulements turbulents gaz‐particules. En outre, l'interaction collisionnelle entre les particules est modèlisée à l'aide de la théorie cinétique des écoulements granulaires reposant sur la théorie des gaz denses de Chapman‐Enskog. La comparaison avec les résultats expérimentaux de Miller et Gidsprow (1 992) montre un accord raisonnablement bon. Le modèle présent peut fournier une approche utile pour la prédiction du comportement hydrodynamique complexe des systèmes de lits fluidisés. |
doi_str_mv | 10.1002/cjce.5450770605 |
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Un nouveau modèle numérique utilisant à la fois des coordonnées eulériennes et lagrangiennes et tenant compte desinteractions entre les particules a été mis au point pour l'étude des aspects hydrodynamiques d'écoulements ascendants chargés de particules denses. Un modèle de dispersion de particules stochastique est introduit au modèle original afin de décrire les écoulements turbulents gaz‐particules. En outre, l'interaction collisionnelle entre les particules est modèlisée à l'aide de la théorie cinétique des écoulements granulaires reposant sur la théorie des gaz denses de Chapman‐Enskog. La comparaison avec les résultats expérimentaux de Miller et Gidsprow (1 992) montre un accord raisonnablement bon. Le modèle présent peut fournier une approche utile pour la prédiction du comportement hydrodynamique complexe des systèmes de lits fluidisés.</description><identifier>ISSN: 0008-4034</identifier><identifier>EISSN: 1939-019X</identifier><identifier>DOI: 10.1002/cjce.5450770605</identifier><identifier>CODEN: CJCEA7</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc., A Wiley Company</publisher><subject>Computational methods in fluid dynamics ; dense particle-laden rise flows ; Eulerian/Lagrangian approach ; Exact sciences and technology ; Fluid dynamics ; Fundamental areas of phenomenology (including applications) ; interparticle collision ; Multiphase and particle-laden flows ; Nonhomogeneous flows ; Physics</subject><ispartof>Canadian journal of chemical engineering, 1999-12, Vol.77 (6), p.1113-1120</ispartof><rights>Copyright © 1999 Canadian Society for Chemical Engineering</rights><rights>2000 INIST-CNRS</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c3535-9ad04dbc08635c8fe018ba135a7d4d6bce73b0f8d9404485c5d02338258b5bde3</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%2Fcjce.5450770605$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fcjce.5450770605$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1417,27924,27925,45574,45575</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=1258694$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Fan, Jianren</creatorcontrib><creatorcontrib>Sun, Ping</creatorcontrib><creatorcontrib>Ma, Yinliang</creatorcontrib><creatorcontrib>Cen, Kefa</creatorcontrib><title>On a eulerian and lagrangian combined model in dense particle-laden riser flow</title><title>Canadian journal of chemical engineering</title><addtitle>Can. J. Chem. Eng</addtitle><description>A new numerical model using both Eulerian and Lagrangian coordinates, and taking account of interparticle interactions, has been developed for the study of hydrodynamic aspects of dense particle‐laden rise flows. A stochastic particle dispersion model has been incorporated in the original model to describe the gas particle turbulent flows. In addition, the collisional interaction between the particles has been modeled using the kinetic theory of granular flows based on the Chapman‐Enskog theory of dense gases. A comparison with the experimental results of Miller and Gidspow (1992) shows reasonably good agreement. The present model may provide a useful approach for predicting the complex hydrodynamic behaviour of fluidized bed systems.
Un nouveau modèle numérique utilisant à la fois des coordonnées eulériennes et lagrangiennes et tenant compte desinteractions entre les particules a été mis au point pour l'étude des aspects hydrodynamiques d'écoulements ascendants chargés de particules denses. Un modèle de dispersion de particules stochastique est introduit au modèle original afin de décrire les écoulements turbulents gaz‐particules. En outre, l'interaction collisionnelle entre les particules est modèlisée à l'aide de la théorie cinétique des écoulements granulaires reposant sur la théorie des gaz denses de Chapman‐Enskog. La comparaison avec les résultats expérimentaux de Miller et Gidsprow (1 992) montre un accord raisonnablement bon. Le modèle présent peut fournier une approche utile pour la prédiction du comportement hydrodynamique complexe des systèmes de lits fluidisés.</description><subject>Computational methods in fluid dynamics</subject><subject>dense particle-laden rise flows</subject><subject>Eulerian/Lagrangian approach</subject><subject>Exact sciences and technology</subject><subject>Fluid dynamics</subject><subject>Fundamental areas of phenomenology (including applications)</subject><subject>interparticle collision</subject><subject>Multiphase and particle-laden flows</subject><subject>Nonhomogeneous flows</subject><subject>Physics</subject><issn>0008-4034</issn><issn>1939-019X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1999</creationdate><recordtype>article</recordtype><recordid>eNqFkDtPwzAUhS0EEqUws3pgDb2u7cQRE0SlPKqWoQg2y7GdysVNKruo9N-TKoiKiek-dL5zdQ9ClwSuCcBwoJfaXnPGIcsgBX6EeiSneQIkfz9GPQAQCQPKTtFZjMt2HAIjPTSd1Vhh--ltcKpta4O9WgRVL_ajblalq63Bq8ZYj12Nja2jxWsVNk57m3jVLnBw0QZc-WZ7jk4q5aO9-Kl99Ho_mhcPyWQ2fixuJ4mmnPIkVwaYKTWIlHItKgtElIpQrjLDTFpqm9ESKmFyBowJrrmBIaViyEXJS2NpHw06Xx2aGIOt5Dq4lQo7SUDu45D7OOQhjpa46oi1ilr5qn1Ru3jAWus0Z63sppNtnbe7_1xl8VSM_hxJOtrFjf36pVX4kGlGMy7fpmN5J-ZTnr0I-Uy_AdUCgHA</recordid><startdate>199912</startdate><enddate>199912</enddate><creator>Fan, Jianren</creator><creator>Sun, Ping</creator><creator>Ma, Yinliang</creator><creator>Cen, Kefa</creator><general>Wiley Subscription Services, Inc., A Wiley Company</general><general>Wiley</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>199912</creationdate><title>On a eulerian and lagrangian combined model in dense particle-laden riser flow</title><author>Fan, Jianren ; Sun, Ping ; Ma, Yinliang ; Cen, Kefa</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3535-9ad04dbc08635c8fe018ba135a7d4d6bce73b0f8d9404485c5d02338258b5bde3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1999</creationdate><topic>Computational methods in fluid dynamics</topic><topic>dense particle-laden rise flows</topic><topic>Eulerian/Lagrangian approach</topic><topic>Exact sciences and technology</topic><topic>Fluid dynamics</topic><topic>Fundamental areas of phenomenology (including applications)</topic><topic>interparticle collision</topic><topic>Multiphase and particle-laden flows</topic><topic>Nonhomogeneous flows</topic><topic>Physics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Fan, Jianren</creatorcontrib><creatorcontrib>Sun, Ping</creatorcontrib><creatorcontrib>Ma, Yinliang</creatorcontrib><creatorcontrib>Cen, Kefa</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>Canadian journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Fan, Jianren</au><au>Sun, Ping</au><au>Ma, Yinliang</au><au>Cen, Kefa</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>On a eulerian and lagrangian combined model in dense particle-laden riser flow</atitle><jtitle>Canadian journal of chemical engineering</jtitle><addtitle>Can. J. Chem. Eng</addtitle><date>1999-12</date><risdate>1999</risdate><volume>77</volume><issue>6</issue><spage>1113</spage><epage>1120</epage><pages>1113-1120</pages><issn>0008-4034</issn><eissn>1939-019X</eissn><coden>CJCEA7</coden><abstract>A new numerical model using both Eulerian and Lagrangian coordinates, and taking account of interparticle interactions, has been developed for the study of hydrodynamic aspects of dense particle‐laden rise flows. A stochastic particle dispersion model has been incorporated in the original model to describe the gas particle turbulent flows. In addition, the collisional interaction between the particles has been modeled using the kinetic theory of granular flows based on the Chapman‐Enskog theory of dense gases. A comparison with the experimental results of Miller and Gidspow (1992) shows reasonably good agreement. The present model may provide a useful approach for predicting the complex hydrodynamic behaviour of fluidized bed systems.
Un nouveau modèle numérique utilisant à la fois des coordonnées eulériennes et lagrangiennes et tenant compte desinteractions entre les particules a été mis au point pour l'étude des aspects hydrodynamiques d'écoulements ascendants chargés de particules denses. Un modèle de dispersion de particules stochastique est introduit au modèle original afin de décrire les écoulements turbulents gaz‐particules. En outre, l'interaction collisionnelle entre les particules est modèlisée à l'aide de la théorie cinétique des écoulements granulaires reposant sur la théorie des gaz denses de Chapman‐Enskog. La comparaison avec les résultats expérimentaux de Miller et Gidsprow (1 992) montre un accord raisonnablement bon. Le modèle présent peut fournier une approche utile pour la prédiction du comportement hydrodynamique complexe des systèmes de lits fluidisés.</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc., A Wiley Company</pub><doi>10.1002/cjce.5450770605</doi><tpages>8</tpages><oa>free_for_read</oa></addata></record> |
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subjects | Computational methods in fluid dynamics dense particle-laden rise flows Eulerian/Lagrangian approach Exact sciences and technology Fluid dynamics Fundamental areas of phenomenology (including applications) interparticle collision Multiphase and particle-laden flows Nonhomogeneous flows Physics |
title | On a eulerian and lagrangian combined model in dense particle-laden riser flow |
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