Cargando…

Experimental and Numerical Simulation Study of Devolatilization in a Self-Wiping Corotating Parallel Twin-Screw Extruder

Devolatilization is an important process for separating and removing unnecessary residual volatile substances or solvents during the production of polymers using twin-screw extruders. Latinen proposed a surface renewal model to determine the concentration of volatile components in the extrudate of a...

Descripción completa

Detalles Bibliográficos
Autores principales: Ohara, Masatoshi, Sasai, Yuya, Umemoto, Sho, Obata, Yuya, Sugiyama, Takemasa, Tanifuji, Shin-ichiro, Kihara, Shin-ichi, Taki, Kentaro
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2020
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7698560/
https://www.ncbi.nlm.nih.gov/pubmed/33213055
http://dx.doi.org/10.3390/polym12112728
_version_ 1783615859734872064
author Ohara, Masatoshi
Sasai, Yuya
Umemoto, Sho
Obata, Yuya
Sugiyama, Takemasa
Tanifuji, Shin-ichiro
Kihara, Shin-ichi
Taki, Kentaro
author_facet Ohara, Masatoshi
Sasai, Yuya
Umemoto, Sho
Obata, Yuya
Sugiyama, Takemasa
Tanifuji, Shin-ichiro
Kihara, Shin-ichi
Taki, Kentaro
author_sort Ohara, Masatoshi
collection PubMed
description Devolatilization is an important process for separating and removing unnecessary residual volatile substances or solvents during the production of polymers using twin-screw extruders. Latinen proposed a surface renewal model to determine the concentration of volatile components in the extrudate of a single-screw extruder. When a twin-screw extruder is used to calculate the concentration, it is necessary to use the exposed surface area of the resin in the starved region of Latinen’s model, which, however, is difficult to estimate. In our previous work, we numerically determined resin profiles of the screws using the 2.5D Hele–Shaw flow model and the finite element method, which helps in estimating the surface area of devolatilization. In this study, we numerically analyzed the volatile concentration of the extrudate in a self-wiping corotating twin-screw extruder using Latinen’s surface renewal model along with our resin profile calculation method. The experimental results of the concentrations of the volatile component (toluene) in the extrudate of polypropylene agreed well with its numerical calculation with a relative error of 6.5% (except for the data of the lowest rotational speed). Our results also showed that decreasing the flow rate and increasing the pump capacity were effective for removing the volatile component. The screw pitch of a full-flight screw was not affected by the devolatilization efficiency with a fixed flow rate and screw speed.
format Online
Article
Text
id pubmed-7698560
institution National Center for Biotechnology Information
language English
publishDate 2020
publisher MDPI
record_format MEDLINE/PubMed
spelling pubmed-76985602020-11-29 Experimental and Numerical Simulation Study of Devolatilization in a Self-Wiping Corotating Parallel Twin-Screw Extruder Ohara, Masatoshi Sasai, Yuya Umemoto, Sho Obata, Yuya Sugiyama, Takemasa Tanifuji, Shin-ichiro Kihara, Shin-ichi Taki, Kentaro Polymers (Basel) Article Devolatilization is an important process for separating and removing unnecessary residual volatile substances or solvents during the production of polymers using twin-screw extruders. Latinen proposed a surface renewal model to determine the concentration of volatile components in the extrudate of a single-screw extruder. When a twin-screw extruder is used to calculate the concentration, it is necessary to use the exposed surface area of the resin in the starved region of Latinen’s model, which, however, is difficult to estimate. In our previous work, we numerically determined resin profiles of the screws using the 2.5D Hele–Shaw flow model and the finite element method, which helps in estimating the surface area of devolatilization. In this study, we numerically analyzed the volatile concentration of the extrudate in a self-wiping corotating twin-screw extruder using Latinen’s surface renewal model along with our resin profile calculation method. The experimental results of the concentrations of the volatile component (toluene) in the extrudate of polypropylene agreed well with its numerical calculation with a relative error of 6.5% (except for the data of the lowest rotational speed). Our results also showed that decreasing the flow rate and increasing the pump capacity were effective for removing the volatile component. The screw pitch of a full-flight screw was not affected by the devolatilization efficiency with a fixed flow rate and screw speed. MDPI 2020-11-17 /pmc/articles/PMC7698560/ /pubmed/33213055 http://dx.doi.org/10.3390/polym12112728 Text en © 2020 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Ohara, Masatoshi
Sasai, Yuya
Umemoto, Sho
Obata, Yuya
Sugiyama, Takemasa
Tanifuji, Shin-ichiro
Kihara, Shin-ichi
Taki, Kentaro
Experimental and Numerical Simulation Study of Devolatilization in a Self-Wiping Corotating Parallel Twin-Screw Extruder
title Experimental and Numerical Simulation Study of Devolatilization in a Self-Wiping Corotating Parallel Twin-Screw Extruder
title_full Experimental and Numerical Simulation Study of Devolatilization in a Self-Wiping Corotating Parallel Twin-Screw Extruder
title_fullStr Experimental and Numerical Simulation Study of Devolatilization in a Self-Wiping Corotating Parallel Twin-Screw Extruder
title_full_unstemmed Experimental and Numerical Simulation Study of Devolatilization in a Self-Wiping Corotating Parallel Twin-Screw Extruder
title_short Experimental and Numerical Simulation Study of Devolatilization in a Self-Wiping Corotating Parallel Twin-Screw Extruder
title_sort experimental and numerical simulation study of devolatilization in a self-wiping corotating parallel twin-screw extruder
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7698560/
https://www.ncbi.nlm.nih.gov/pubmed/33213055
http://dx.doi.org/10.3390/polym12112728
work_keys_str_mv AT oharamasatoshi experimentalandnumericalsimulationstudyofdevolatilizationinaselfwipingcorotatingparalleltwinscrewextruder
AT sasaiyuya experimentalandnumericalsimulationstudyofdevolatilizationinaselfwipingcorotatingparalleltwinscrewextruder
AT umemotosho experimentalandnumericalsimulationstudyofdevolatilizationinaselfwipingcorotatingparalleltwinscrewextruder
AT obatayuya experimentalandnumericalsimulationstudyofdevolatilizationinaselfwipingcorotatingparalleltwinscrewextruder
AT sugiyamatakemasa experimentalandnumericalsimulationstudyofdevolatilizationinaselfwipingcorotatingparalleltwinscrewextruder
AT tanifujishinichiro experimentalandnumericalsimulationstudyofdevolatilizationinaselfwipingcorotatingparalleltwinscrewextruder
AT kiharashinichi experimentalandnumericalsimulationstudyofdevolatilizationinaselfwipingcorotatingparalleltwinscrewextruder
AT takikentaro experimentalandnumericalsimulationstudyofdevolatilizationinaselfwipingcorotatingparalleltwinscrewextruder