Study of droplet size distribution during an emulsification process using in situ video probe coupled with an automatic image analysis
Understanding the evolution of liquid–liquid dispersion is a key factor in operation and control of emulsification process. A dynamic tracking of an evolving droplet size distribution (DSD) in a dilute oil-in water (O/W) emulsion has been developed with the implementation of an in situ video probe d...
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Veröffentlicht in: | Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2010-12, Vol.165 (3), p.946-957 |
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creator | Khalil, Abir Puel, François Chevalier, Yves Galvan, Jean-Marc Rivoire, Alain Klein, Jean-Paul |
description | Understanding the evolution of liquid–liquid dispersion is a key factor in operation and control of emulsification process. A dynamic tracking of an evolving droplet size distribution (DSD) in a dilute oil-in water (O/W) emulsion has been developed with the implementation of an
in situ video probe dipped in a stirred vessel and coupled with an image analysis treatment. The optical probe allows real time recording of 2D images of the droplets. Recent image analysis software developed originally for an application in micromechanics was adapted and applied in delayed time on the video sequences regularly recorded. It automatically provided a measurement of the diameter of several thousands of droplets in the range of 10–100
μm. The relative accuracy on the droplet number average diameter was 10%. This measurement technique was then used to investigate at lab scale in a stirred vessel and in warm conditions the influence of several process parameters on the evolution with time of a dispersed melted cosmetic ingredient in a water solution containing a surfactant. The specific power input of stirring was the main parameter acting on the reduction of the mean droplet diameter and of the width of the DSD owing to its action on the droplet break-up mechanism. The surfactant concentration was a parameter of secondary relevance on the DSD probably due to the reduction of the coalescence rate and to a faster stabilization of the O/W interface. The use of a flat blade propeller instead of a Rushton turbine was preferable for the production of a narrower DSD. Finally the time required to reach equilibrium was found higher by a factor of 3–4 than predicted in the literature. |
doi_str_mv | 10.1016/j.cej.2010.10.031 |
format | Article |
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μm. The relative accuracy on the droplet number average diameter was 10%. This measurement technique was then used to investigate at lab scale in a stirred vessel and in warm conditions the influence of several process parameters on the evolution with time of a dispersed melted cosmetic ingredient in a water solution containing a surfactant. The specific power input of stirring was the main parameter acting on the reduction of the mean droplet diameter and of the width of the DSD owing to its action on the droplet break-up mechanism. The surfactant concentration was a parameter of secondary relevance on the DSD probably due to the reduction of the coalescence rate and to a faster stabilization of the O/W interface. The use of a flat blade propeller instead of a Rushton turbine was preferable for the production of a narrower DSD. Finally the time required to reach equilibrium was found higher by a factor of 3–4 than predicted in the literature.</description><identifier>ISSN: 1385-8947</identifier><identifier>EISSN: 1873-3212</identifier><identifier>DOI: 10.1016/j.cej.2010.10.031</identifier><language>eng</language><publisher>Oxford: Elsevier B.V</publisher><subject>Applied sciences ; Chemical and Process Engineering ; Chemical engineering ; Chemical Sciences ; Chemistry ; Colloidal state and disperse state ; Computer programs ; Drop size measurement ; Emulsification process ; Engineering Sciences ; Exact sciences and technology ; Galenic pharmacology ; General and physical chemistry ; Image analysis ; in situ monitoring ; Life Sciences ; Material chemistry ; Mixing ; Multiphase mixing ; or physical chemistry ; Pharmaceutical sciences ; Physical and chemical studies. Granulometry. Electrokinetic phenomena ; Polymers ; Stirred vessel ; Theoretical and</subject><ispartof>Chemical engineering journal (Lausanne, Switzerland : 1996), 2010-12, Vol.165 (3), p.946-957</ispartof><rights>2010 Elsevier B.V.</rights><rights>2015 INIST-CNRS</rights><rights>Distributed under a Creative Commons Attribution 4.0 International License</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c393t-c70816cdbfd5801facfb070be5022cff4f3336a9d5ab490ea81efe147d7aea983</citedby><cites>FETCH-LOGICAL-c393t-c70816cdbfd5801facfb070be5022cff4f3336a9d5ab490ea81efe147d7aea983</cites><orcidid>0000-0002-7526-5658 ; 0000-0001-6059-7273</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.cej.2010.10.031$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>230,314,777,781,882,3538,27906,27907,45977</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=23635866$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://hal.science/hal-02844838$$DView record in HAL$$Hfree_for_read</backlink></links><search><creatorcontrib>Khalil, Abir</creatorcontrib><creatorcontrib>Puel, François</creatorcontrib><creatorcontrib>Chevalier, Yves</creatorcontrib><creatorcontrib>Galvan, Jean-Marc</creatorcontrib><creatorcontrib>Rivoire, Alain</creatorcontrib><creatorcontrib>Klein, Jean-Paul</creatorcontrib><title>Study of droplet size distribution during an emulsification process using in situ video probe coupled with an automatic image analysis</title><title>Chemical engineering journal (Lausanne, Switzerland : 1996)</title><description>Understanding the evolution of liquid–liquid dispersion is a key factor in operation and control of emulsification process. A dynamic tracking of an evolving droplet size distribution (DSD) in a dilute oil-in water (O/W) emulsion has been developed with the implementation of an
in situ video probe dipped in a stirred vessel and coupled with an image analysis treatment. The optical probe allows real time recording of 2D images of the droplets. Recent image analysis software developed originally for an application in micromechanics was adapted and applied in delayed time on the video sequences regularly recorded. It automatically provided a measurement of the diameter of several thousands of droplets in the range of 10–100
μm. The relative accuracy on the droplet number average diameter was 10%. This measurement technique was then used to investigate at lab scale in a stirred vessel and in warm conditions the influence of several process parameters on the evolution with time of a dispersed melted cosmetic ingredient in a water solution containing a surfactant. The specific power input of stirring was the main parameter acting on the reduction of the mean droplet diameter and of the width of the DSD owing to its action on the droplet break-up mechanism. The surfactant concentration was a parameter of secondary relevance on the DSD probably due to the reduction of the coalescence rate and to a faster stabilization of the O/W interface. The use of a flat blade propeller instead of a Rushton turbine was preferable for the production of a narrower DSD. Finally the time required to reach equilibrium was found higher by a factor of 3–4 than predicted in the literature.</description><subject>Applied sciences</subject><subject>Chemical and Process Engineering</subject><subject>Chemical engineering</subject><subject>Chemical Sciences</subject><subject>Chemistry</subject><subject>Colloidal state and disperse state</subject><subject>Computer programs</subject><subject>Drop size measurement</subject><subject>Emulsification process</subject><subject>Engineering Sciences</subject><subject>Exact sciences and technology</subject><subject>Galenic pharmacology</subject><subject>General and physical chemistry</subject><subject>Image analysis</subject><subject>in situ monitoring</subject><subject>Life Sciences</subject><subject>Material chemistry</subject><subject>Mixing</subject><subject>Multiphase mixing</subject><subject>or physical chemistry</subject><subject>Pharmaceutical sciences</subject><subject>Physical and chemical studies. Granulometry. 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Electrokinetic phenomena</topic><topic>Polymers</topic><topic>Stirred vessel</topic><topic>Theoretical and</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Khalil, Abir</creatorcontrib><creatorcontrib>Puel, François</creatorcontrib><creatorcontrib>Chevalier, Yves</creatorcontrib><creatorcontrib>Galvan, Jean-Marc</creatorcontrib><creatorcontrib>Rivoire, Alain</creatorcontrib><creatorcontrib>Klein, Jean-Paul</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Hyper Article en Ligne (HAL)</collection><jtitle>Chemical engineering journal (Lausanne, Switzerland : 1996)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Khalil, Abir</au><au>Puel, François</au><au>Chevalier, Yves</au><au>Galvan, Jean-Marc</au><au>Rivoire, Alain</au><au>Klein, Jean-Paul</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Study of droplet size distribution during an emulsification process using in situ video probe coupled with an automatic image analysis</atitle><jtitle>Chemical engineering journal (Lausanne, Switzerland : 1996)</jtitle><date>2010-12-15</date><risdate>2010</risdate><volume>165</volume><issue>3</issue><spage>946</spage><epage>957</epage><pages>946-957</pages><issn>1385-8947</issn><eissn>1873-3212</eissn><abstract>Understanding the evolution of liquid–liquid dispersion is a key factor in operation and control of emulsification process. 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μm. The relative accuracy on the droplet number average diameter was 10%. This measurement technique was then used to investigate at lab scale in a stirred vessel and in warm conditions the influence of several process parameters on the evolution with time of a dispersed melted cosmetic ingredient in a water solution containing a surfactant. The specific power input of stirring was the main parameter acting on the reduction of the mean droplet diameter and of the width of the DSD owing to its action on the droplet break-up mechanism. The surfactant concentration was a parameter of secondary relevance on the DSD probably due to the reduction of the coalescence rate and to a faster stabilization of the O/W interface. The use of a flat blade propeller instead of a Rushton turbine was preferable for the production of a narrower DSD. Finally the time required to reach equilibrium was found higher by a factor of 3–4 than predicted in the literature.</abstract><cop>Oxford</cop><pub>Elsevier B.V</pub><doi>10.1016/j.cej.2010.10.031</doi><tpages>12</tpages><orcidid>https://orcid.org/0000-0002-7526-5658</orcidid><orcidid>https://orcid.org/0000-0001-6059-7273</orcidid></addata></record> |
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subjects | Applied sciences Chemical and Process Engineering Chemical engineering Chemical Sciences Chemistry Colloidal state and disperse state Computer programs Drop size measurement Emulsification process Engineering Sciences Exact sciences and technology Galenic pharmacology General and physical chemistry Image analysis in situ monitoring Life Sciences Material chemistry Mixing Multiphase mixing or physical chemistry Pharmaceutical sciences Physical and chemical studies. Granulometry. Electrokinetic phenomena Polymers Stirred vessel Theoretical and |
title | Study of droplet size distribution during an emulsification process using in situ video probe coupled with an automatic image analysis |
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