Numerical simulation and experimental validation of mixing performance of kneading discs in a twin screw extruder
Identifieur interne : 000F34 ( Main/Exploration ); précédent : 000F33; suivant : 000F35Numerical simulation and experimental validation of mixing performance of kneading discs in a twin screw extruder
Auteurs : Xian-Ming Zhang [République populaire de Chine] ; Lian-Fang Feng [République populaire de Chine, France] ; Wen-Xing Chen [République populaire de Chine] ; Guo-Hua Hu [France]Source :
- Polymer Engineering & Science [ 0032-3888 ] ; 2009-09.
Descripteurs français
- Pascal (Inist)
- Wicri :
- topic : Polymère, Simulation.
English descriptors
- KwdEn :
- Aiche, Area stretch, Area stretch ratio, Avalosse, Axial, Axial distance, Axial evolution, Carreau model, Computational fluid dynamics, Contract grant number, Contract grant sponsor, Critical value, Critical values, Delay time, Different mixers, Different percentiles, Different regions, Different screw, Different types, Disc, Disc gaps, Disc width, Distributive, Double screw extruder, Experimental data, Experimental ones, Experimental results, Experimental test, Experimental validation, Extruder, Extrusion, Feed rate, Flow channel, Generalized newtonian, Hegi, High percentiles, Important role, Initial direction, Initial stage, Inlet section, Intermeshing, Large amount, Larger disc width, Manufacturing technology, Marker, Marker particle, Marker particles, Material surface, Minimal residence time, Mixer, Mixing quality, Modeling, Normal direction, Numerical simulation, Numerical simulations, Other hand, Outlet section, Outlet sections, Percentile, Polym, Polymer, Polymer engineering, Residence time, Residence time distribution, Same disc width, Screw element, Screw elements, Screw speed, Shear rate, Simulation, Smaller disc width, Statistical theory, Stretch rate, Strong reorientation, Surface area, Test zone, Textile materials, Theoretical study, Twin screw extruders, Virtual particles, Zhejiang university.
- Teeft :
- Aiche, Area stretch, Area stretch ratio, Avalosse, Axial, Axial distance, Axial evolution, Carreau model, Contract grant number, Contract grant sponsor, Critical value, Critical values, Delay time, Different mixers, Different percentiles, Different regions, Different screw, Different types, Disc, Disc gaps, Disc width, Distributive, Experimental data, Experimental ones, Experimental results, Experimental validation, Extruder, Feed rate, Flow channel, Generalized newtonian, Hegi, High percentiles, Important role, Initial direction, Initial stage, Inlet section, Intermeshing, Large amount, Larger disc width, Manufacturing technology, Marker, Marker particle, Marker particles, Material surface, Minimal residence time, Mixer, Normal direction, Numerical simulation, Numerical simulations, Other hand, Outlet section, Outlet sections, Percentile, Polym, Polymer, Polymer engineering, Residence time, Residence time distribution, Same disc width, Screw element, Screw elements, Screw speed, Shear rate, Simulation, Smaller disc width, Statistical theory, Stretch rate, Strong reorientation, Surface area, Test zone, Textile materials, Twin screw extruders, Virtual particles, Zhejiang university.
Abstract
This work aims at simulation by particle tracking the local residence time distributions (RTDs) of a co‐rotating twin‐screw extruder using computational fluid dynamics. Simulated results follow reasonably well the trend of experimental results obtained by an in‐line measuring instrument for different screw configurations and feed rates. To analyze the distributive mixing performance and overall efficiency of different types of kneading discs (KDs), mixing parameters such as area stretch ratio, instantaneous efficiency, and time‐average efficiency are calculated. Among KDs with stagger angles 45°, 60°, and 90°, the 90/10/64 with disc gaps is most efficient in terms of distributive mixing. The effects of the disc width and disc gap on the local RTD and distributive mixing are also discussed. This provides a numerical tool for assessing point‐by‐point information on the local RTD, flow, and mixing along the screw extruder. POLYM. ENG. SCI., 2009. © 2009 Society of Plastics Engineers
Url:
DOI: 10.1002/pen.21404
Affiliations:
- France, République populaire de Chine
- Grand Est, Lorraine (région), Zhejiang, Île-de-France
- Hangzhou, Nancy, Paris
- Centre national de la recherche scientifique, Laboratoire réactions et génie des procédés, Université de Lorraine, Université de Zhejiang
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Le document en format XML
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<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Aiche</term>
<term>Area stretch</term>
<term>Area stretch ratio</term>
<term>Avalosse</term>
<term>Axial</term>
<term>Axial distance</term>
<term>Axial evolution</term>
<term>Carreau model</term>
<term>Computational fluid dynamics</term>
<term>Contract grant number</term>
<term>Contract grant sponsor</term>
<term>Critical value</term>
<term>Critical values</term>
<term>Delay time</term>
<term>Different mixers</term>
<term>Different percentiles</term>
<term>Different regions</term>
<term>Different screw</term>
<term>Different types</term>
<term>Disc</term>
<term>Disc gaps</term>
<term>Disc width</term>
<term>Distributive</term>
<term>Double screw extruder</term>
<term>Experimental data</term>
<term>Experimental ones</term>
<term>Experimental results</term>
<term>Experimental test</term>
<term>Experimental validation</term>
<term>Extruder</term>
<term>Extrusion</term>
<term>Feed rate</term>
<term>Flow channel</term>
<term>Generalized newtonian</term>
<term>Hegi</term>
<term>High percentiles</term>
<term>Important role</term>
<term>Initial direction</term>
<term>Initial stage</term>
<term>Inlet section</term>
<term>Intermeshing</term>
<term>Large amount</term>
<term>Larger disc width</term>
<term>Manufacturing technology</term>
<term>Marker</term>
<term>Marker particle</term>
<term>Marker particles</term>
<term>Material surface</term>
<term>Minimal residence time</term>
<term>Mixer</term>
<term>Mixing quality</term>
<term>Modeling</term>
<term>Normal direction</term>
<term>Numerical simulation</term>
<term>Numerical simulations</term>
<term>Other hand</term>
<term>Outlet section</term>
<term>Outlet sections</term>
<term>Percentile</term>
<term>Polym</term>
<term>Polymer</term>
<term>Polymer engineering</term>
<term>Residence time</term>
<term>Residence time distribution</term>
<term>Same disc width</term>
<term>Screw element</term>
<term>Screw elements</term>
<term>Screw speed</term>
<term>Shear rate</term>
<term>Simulation</term>
<term>Smaller disc width</term>
<term>Statistical theory</term>
<term>Stretch rate</term>
<term>Strong reorientation</term>
<term>Surface area</term>
<term>Test zone</term>
<term>Textile materials</term>
<term>Theoretical study</term>
<term>Twin screw extruders</term>
<term>Virtual particles</term>
<term>Zhejiang university</term>
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<keywords scheme="Pascal" xml:lang="fr"><term>Disques malaxage</term>
<term>Distribution temps séjour</term>
<term>Etude théorique</term>
<term>Extrusion</term>
<term>Modélisation</term>
<term>Mécanique fluide numérique</term>
<term>Polymère</term>
<term>Presse extrusion double vis</term>
<term>Presse extrusion double vis co-rotative</term>
<term>Qualité mélangeage</term>
<term>Simulation numérique</term>
<term>Vérification expérimentale</term>
</keywords>
<keywords scheme="Teeft" xml:lang="en"><term>Aiche</term>
<term>Area stretch</term>
<term>Area stretch ratio</term>
<term>Avalosse</term>
<term>Axial</term>
<term>Axial distance</term>
<term>Axial evolution</term>
<term>Carreau model</term>
<term>Contract grant number</term>
<term>Contract grant sponsor</term>
<term>Critical value</term>
<term>Critical values</term>
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<term>Different regions</term>
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<term>Different types</term>
<term>Disc</term>
<term>Disc gaps</term>
<term>Disc width</term>
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<term>Experimental data</term>
<term>Experimental ones</term>
<term>Experimental results</term>
<term>Experimental validation</term>
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<term>Feed rate</term>
<term>Flow channel</term>
<term>Generalized newtonian</term>
<term>Hegi</term>
<term>High percentiles</term>
<term>Important role</term>
<term>Initial direction</term>
<term>Initial stage</term>
<term>Inlet section</term>
<term>Intermeshing</term>
<term>Large amount</term>
<term>Larger disc width</term>
<term>Manufacturing technology</term>
<term>Marker</term>
<term>Marker particle</term>
<term>Marker particles</term>
<term>Material surface</term>
<term>Minimal residence time</term>
<term>Mixer</term>
<term>Normal direction</term>
<term>Numerical simulation</term>
<term>Numerical simulations</term>
<term>Other hand</term>
<term>Outlet section</term>
<term>Outlet sections</term>
<term>Percentile</term>
<term>Polym</term>
<term>Polymer</term>
<term>Polymer engineering</term>
<term>Residence time</term>
<term>Residence time distribution</term>
<term>Same disc width</term>
<term>Screw element</term>
<term>Screw elements</term>
<term>Screw speed</term>
<term>Shear rate</term>
<term>Simulation</term>
<term>Smaller disc width</term>
<term>Statistical theory</term>
<term>Stretch rate</term>
<term>Strong reorientation</term>
<term>Surface area</term>
<term>Test zone</term>
<term>Textile materials</term>
<term>Twin screw extruders</term>
<term>Virtual particles</term>
<term>Zhejiang university</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr"><term>Polymère</term>
<term>Simulation</term>
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<front><div type="abstract" xml:lang="en">This work aims at simulation by particle tracking the local residence time distributions (RTDs) of a co‐rotating twin‐screw extruder using computational fluid dynamics. Simulated results follow reasonably well the trend of experimental results obtained by an in‐line measuring instrument for different screw configurations and feed rates. To analyze the distributive mixing performance and overall efficiency of different types of kneading discs (KDs), mixing parameters such as area stretch ratio, instantaneous efficiency, and time‐average efficiency are calculated. Among KDs with stagger angles 45°, 60°, and 90°, the 90/10/64 with disc gaps is most efficient in terms of distributive mixing. The effects of the disc width and disc gap on the local RTD and distributive mixing are also discussed. This provides a numerical tool for assessing point‐by‐point information on the local RTD, flow, and mixing along the screw extruder. POLYM. ENG. SCI., 2009. © 2009 Society of Plastics Engineers</div>
</front>
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<country name="France"><region name="Grand Est"><name sortKey="Feng, Lian Ang" sort="Feng, Lian Ang" uniqKey="Feng L" first="Lian-Fang" last="Feng">Lian-Fang Feng</name>
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