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Numerical simulation and experimental validation of mixing performance of kneading discs in a twin screw extruder

Identifieur interne : 000F34 ( Main/Exploration ); précédent : 000F33; suivant : 000F35

Numerical 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]

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RBID : ISTEX:CF792276482E693A042AD6FDF60A705AF5A1A105

Descripteurs français

English descriptors

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


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<term>Axial</term>
<term>Axial distance</term>
<term>Axial evolution</term>
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<term>Double screw extruder</term>
<term>Experimental data</term>
<term>Experimental ones</term>
<term>Experimental results</term>
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<term>Experimental validation</term>
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<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>
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<term>Normal direction</term>
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<term>Numerical simulations</term>
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<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>
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<term>Screw element</term>
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<term>Virtual particles</term>
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<term>Disques malaxage</term>
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<term>Modélisation</term>
<term>Mécanique fluide numérique</term>
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<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>
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<term>Area stretch</term>
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<term>Simulation</term>
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<term>Surface area</term>
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<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>
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