On the relative motion of a particle in a swarm of different particles
The classification of dissimilar particles in a liquid suspension is exploited in many industrial unit operations. To understand and predict fluidization phenomena in general and particle classification in particular, adequate expressions for each of the governing forces—gravity, buoyancy and drag f...
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Veröffentlicht in: | Chemical engineering science 1996, Vol.51 (6), p.995-1008 |
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description | The classification of dissimilar particles in a liquid suspension is exploited in many industrial unit operations. To understand and predict fluidization phenomena in general and particle classification in particular, adequate expressions for each of the governing forces—gravity, buoyancy and drag forces—are required. A possible formulation of the effective driving force and friction in multicomponent mixtures is discussed in this paper. A new expression is derived, which is based on a steady-state force balance for the classifying particle. The expression requires only the usual fluidization data of a single particle species such as the terminal velocity and the Richardson and Zaki index. The new expression is compared with some existing classification models with respect to their predictive value for a wide range of classification data. The new expression proved to be accurate over the entire range of known experimental data and can be extended easily to multicomponent fluidized suspensions. We have found strong evidence that the exact formulation of the buoyancy acting on the classifying particle originates from the bulk density of the fluidized suspension, regardless of the ratio of particle sizes. To clarify the relation between the “overall” drag force and the ratio of particle sizes, the “overall” friction on the classifying particle is decomposed into a solid-liquid and a solid-solid component. The particle-particle interaction force is proportional to the product of the hold-up of the fluidized particles and the slip velocity of dense and fluidized particles. In agreement with other authors, we found an increased friction with a decreasing ratio of classifying and fluidized particles. The particle-particle interaction coefficient was correlated with a modified Stokes-Einstein equation. |
doi_str_mv | 10.1016/0009-2509(95)00343-6 |
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To understand and predict fluidization phenomena in general and particle classification in particular, adequate expressions for each of the governing forces—gravity, buoyancy and drag forces—are required. A possible formulation of the effective driving force and friction in multicomponent mixtures is discussed in this paper. A new expression is derived, which is based on a steady-state force balance for the classifying particle. The expression requires only the usual fluidization data of a single particle species such as the terminal velocity and the Richardson and Zaki index. The new expression is compared with some existing classification models with respect to their predictive value for a wide range of classification data. The new expression proved to be accurate over the entire range of known experimental data and can be extended easily to multicomponent fluidized suspensions. We have found strong evidence that the exact formulation of the buoyancy acting on the classifying particle originates from the bulk density of the fluidized suspension, regardless of the ratio of particle sizes. To clarify the relation between the “overall” drag force and the ratio of particle sizes, the “overall” friction on the classifying particle is decomposed into a solid-liquid and a solid-solid component. The particle-particle interaction force is proportional to the product of the hold-up of the fluidized particles and the slip velocity of dense and fluidized particles. In agreement with other authors, we found an increased friction with a decreasing ratio of classifying and fluidized particles. The particle-particle interaction coefficient was correlated with a modified Stokes-Einstein equation.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/0009-2509(95)00343-6</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Buoyancy ; Chemical engineering ; Correlation methods ; Density (specific gravity) ; Drag ; Exact sciences and technology ; Fluidization ; Friction ; Gravitation ; Industrial applications ; Mathematical models ; Particles (particulate matter) ; Suspensions (fluids) ; Velocity</subject><ispartof>Chemical engineering science, 1996, Vol.51 (6), p.995-1008</ispartof><rights>1996</rights><rights>1996 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c401t-757bec9df425af954f16fc91ee160b76d9eea131b5f02e1fcea482f1b653056c3</citedby><cites>FETCH-LOGICAL-c401t-757bec9df425af954f16fc91ee160b76d9eea131b5f02e1fcea482f1b653056c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/0009-2509(95)00343-6$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,777,781,3537,4010,27904,27905,27906,45976</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=2998125$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Van Der Wielen, L.A.M.</creatorcontrib><creatorcontrib>Van Dam, M.H.H.</creatorcontrib><creatorcontrib>Luyben, K.Ch.A.M.</creatorcontrib><title>On the relative motion of a particle in a swarm of different particles</title><title>Chemical engineering science</title><description>The classification of dissimilar particles in a liquid suspension is exploited in many industrial unit operations. To understand and predict fluidization phenomena in general and particle classification in particular, adequate expressions for each of the governing forces—gravity, buoyancy and drag forces—are required. A possible formulation of the effective driving force and friction in multicomponent mixtures is discussed in this paper. A new expression is derived, which is based on a steady-state force balance for the classifying particle. The expression requires only the usual fluidization data of a single particle species such as the terminal velocity and the Richardson and Zaki index. The new expression is compared with some existing classification models with respect to their predictive value for a wide range of classification data. The new expression proved to be accurate over the entire range of known experimental data and can be extended easily to multicomponent fluidized suspensions. We have found strong evidence that the exact formulation of the buoyancy acting on the classifying particle originates from the bulk density of the fluidized suspension, regardless of the ratio of particle sizes. To clarify the relation between the “overall” drag force and the ratio of particle sizes, the “overall” friction on the classifying particle is decomposed into a solid-liquid and a solid-solid component. The particle-particle interaction force is proportional to the product of the hold-up of the fluidized particles and the slip velocity of dense and fluidized particles. In agreement with other authors, we found an increased friction with a decreasing ratio of classifying and fluidized particles. The particle-particle interaction coefficient was correlated with a modified Stokes-Einstein equation.</description><subject>Applied sciences</subject><subject>Buoyancy</subject><subject>Chemical engineering</subject><subject>Correlation methods</subject><subject>Density (specific gravity)</subject><subject>Drag</subject><subject>Exact sciences and technology</subject><subject>Fluidization</subject><subject>Friction</subject><subject>Gravitation</subject><subject>Industrial applications</subject><subject>Mathematical models</subject><subject>Particles (particulate matter)</subject><subject>Suspensions (fluids)</subject><subject>Velocity</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1996</creationdate><recordtype>article</recordtype><recordid>eNp9kM1LAzEQxYMoWKv_gYc9COphNbObj-YiSLEqFHrRc8hmJxjZj5qkFf97d23p0dPwmN-bxzxCLoHeAQVxTylVecGpulH8ltKSlbk4IhOYyTJnjPJjMjkgp-Qsxs9BSgl0QharLksfmAVsTPJbzNo--b7LepeZbG1C8rbBzHeDit8mtOOi9s5hwC4dgHhOTpxpIl7s55S8L57e5i_5cvX8On9c5pZRSLnkskKrascKbpzizIFwVgEiCFpJUStEAyVU3NECwVk0bFY4qAQvKRe2nJLr3d116L82GJNufbTYNKbDfhO1ZFwyyYUYSLYjbehjDOj0OvjWhB8NVI-t6bESPVaiFdd_renRdrUPMNGaxgXTWR8P3kKpGRR8wB52GA7Pbj0GHa3HzmLtA9qk697_n_MLPQ9_zg</recordid><startdate>1996</startdate><enddate>1996</enddate><creator>Van Der Wielen, L.A.M.</creator><creator>Van Dam, M.H.H.</creator><creator>Luyben, K.Ch.A.M.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TC</scope></search><sort><creationdate>1996</creationdate><title>On the relative motion of a particle in a swarm of different particles</title><author>Van Der Wielen, L.A.M. ; Van Dam, M.H.H. ; Luyben, K.Ch.A.M.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c401t-757bec9df425af954f16fc91ee160b76d9eea131b5f02e1fcea482f1b653056c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1996</creationdate><topic>Applied sciences</topic><topic>Buoyancy</topic><topic>Chemical engineering</topic><topic>Correlation methods</topic><topic>Density (specific gravity)</topic><topic>Drag</topic><topic>Exact sciences and technology</topic><topic>Fluidization</topic><topic>Friction</topic><topic>Gravitation</topic><topic>Industrial applications</topic><topic>Mathematical models</topic><topic>Particles (particulate matter)</topic><topic>Suspensions (fluids)</topic><topic>Velocity</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Van Der Wielen, L.A.M.</creatorcontrib><creatorcontrib>Van Dam, M.H.H.</creatorcontrib><creatorcontrib>Luyben, K.Ch.A.M.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical Engineering Abstracts</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Van Der Wielen, L.A.M.</au><au>Van Dam, M.H.H.</au><au>Luyben, K.Ch.A.M.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>On the relative motion of a particle in a swarm of different particles</atitle><jtitle>Chemical engineering science</jtitle><date>1996</date><risdate>1996</risdate><volume>51</volume><issue>6</issue><spage>995</spage><epage>1008</epage><pages>995-1008</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>The classification of dissimilar particles in a liquid suspension is exploited in many industrial unit operations. To understand and predict fluidization phenomena in general and particle classification in particular, adequate expressions for each of the governing forces—gravity, buoyancy and drag forces—are required. A possible formulation of the effective driving force and friction in multicomponent mixtures is discussed in this paper. A new expression is derived, which is based on a steady-state force balance for the classifying particle. The expression requires only the usual fluidization data of a single particle species such as the terminal velocity and the Richardson and Zaki index. The new expression is compared with some existing classification models with respect to their predictive value for a wide range of classification data. The new expression proved to be accurate over the entire range of known experimental data and can be extended easily to multicomponent fluidized suspensions. We have found strong evidence that the exact formulation of the buoyancy acting on the classifying particle originates from the bulk density of the fluidized suspension, regardless of the ratio of particle sizes. To clarify the relation between the “overall” drag force and the ratio of particle sizes, the “overall” friction on the classifying particle is decomposed into a solid-liquid and a solid-solid component. The particle-particle interaction force is proportional to the product of the hold-up of the fluidized particles and the slip velocity of dense and fluidized particles. In agreement with other authors, we found an increased friction with a decreasing ratio of classifying and fluidized particles. The particle-particle interaction coefficient was correlated with a modified Stokes-Einstein equation.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/0009-2509(95)00343-6</doi><tpages>14</tpages></addata></record> |
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subjects | Applied sciences Buoyancy Chemical engineering Correlation methods Density (specific gravity) Drag Exact sciences and technology Fluidization Friction Gravitation Industrial applications Mathematical models Particles (particulate matter) Suspensions (fluids) Velocity |
title | On the relative motion of a particle in a swarm of different particles |
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