Loading…

Modeling and simulation of the viscoelastic fluid mold filling process by level set method

A model for unifying a viscoelastic fluid and a Newtonian fluid is established, in which the governing equations for the viscoelastic fluid and the Newtonian fluid are successfully united into a system of generalized Navier–Stokes equations. A level set method is set up to solve the model for captur...

Full description

Saved in:
Bibliographic Details
Published in:Journal of non-Newtonian fluid mechanics 2010-10, Vol.165 (19), p.1275-1293
Main Authors: Yang, Binxin, Ouyang, Jie, Li, Qiang, Zhao, Zhifeng, Liu, Chuntai
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Items that cite this one
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by cdi_FETCH-LOGICAL-c365t-c2bff88ab510700e6acd962d55e540497d2d3602451326f8b3b39e9685ee0f0b3
cites cdi_FETCH-LOGICAL-c365t-c2bff88ab510700e6acd962d55e540497d2d3602451326f8b3b39e9685ee0f0b3
container_end_page 1293
container_issue 19
container_start_page 1275
container_title Journal of non-Newtonian fluid mechanics
container_volume 165
creator Yang, Binxin
Ouyang, Jie
Li, Qiang
Zhao, Zhifeng
Liu, Chuntai
description A model for unifying a viscoelastic fluid and a Newtonian fluid is established, in which the governing equations for the viscoelastic fluid and the Newtonian fluid are successfully united into a system of generalized Navier–Stokes equations. A level set method is set up to solve the model for capturing the moving interface in the mold filling process. The physical governing equations are solved by the finite volume method on a non-staggered grid and the interpolation technique on the collocated grid is used for the pressure-velocity and the stress-velocity decoupling problems. The level set and its reinitialization equation are solved by the finite difference method, in which the spatial derivatives are discretized by the 5th-order Weighted Essentially Non-Oscillatory (WENO) scheme, and the temporal derivatives are discretized by the 3rd-order Total Variation Diminishing Runge–Kutta (TVD-R–K) scheme. The validity of the method is verified by some benchmark problems. Then a simulation of viscoelastic fluid mold filling process is pursued with the method. The moving interface and all the information of the physical quantities during the injection process are captured. The die swelling phenomenon is found in the simulation. The influences of elasticity and viscosity on the physical quantities such as stresses etc. in the mold filling process are analyzed. Numerical results show that elastic characteristics such as the stretch and die swelling etc. reinforce accordingly as Weissenberg number increases. Pressures increase continuously in the mold filling process and the pressure maintains the maximum value at the inlet. Injection velocity is proportional to injection pressure. A higher viscosity leads to a higher pressure distribution, that is, the pressure decreases as Reynolds number increases.
doi_str_mv 10.1016/j.jnnfm.2010.06.011
format article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_864419418</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0377025710001680</els_id><sourcerecordid>864419418</sourcerecordid><originalsourceid>FETCH-LOGICAL-c365t-c2bff88ab510700e6acd962d55e540497d2d3602451326f8b3b39e9685ee0f0b3</originalsourceid><addsrcrecordid>eNp9kEFP4zAQha3VIm238Av24gvilDK2Yyc5cFghdkEq4gIXLpZjjxdXTszGaaX-e0yLODKXkUbfm3nzCPnFYMWAqcvNajOOflhxKBNQK2DsG1mwthEVV4J9JwsQTVMBl80P8jPnDZSSQi3I831yGMP4j5rR0RyGbTRzSCNNns4vSHch24TR5DlY6uM2ODqk6KgP8aB6nZLFnGm_pxF3GGnGmQ44vyR3Sk68iRnPPvqSPP25eby-rdYPf--uf68rK5ScK8t779vW9JJBA4DKWNcp7qREWUPdNY47oYDXkgmufNuLXnTYqVYigodeLMnFcW_x8n-LedZDMY0xmhHTNutW1TXratYWUhxJO6WcJ_T6dQqDmfaagX4PUm_0IUj9HqQGpUuQRXX-sd9ka6KfzGhD_pRyIUDwWhTu6shheXYXcNLZBhwtujChnbVL4cs7b65bilE</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>864419418</pqid></control><display><type>article</type><title>Modeling and simulation of the viscoelastic fluid mold filling process by level set method</title><source>ScienceDirect Freedom Collection</source><creator>Yang, Binxin ; Ouyang, Jie ; Li, Qiang ; Zhao, Zhifeng ; Liu, Chuntai</creator><creatorcontrib>Yang, Binxin ; Ouyang, Jie ; Li, Qiang ; Zhao, Zhifeng ; Liu, Chuntai</creatorcontrib><description>A model for unifying a viscoelastic fluid and a Newtonian fluid is established, in which the governing equations for the viscoelastic fluid and the Newtonian fluid are successfully united into a system of generalized Navier–Stokes equations. A level set method is set up to solve the model for capturing the moving interface in the mold filling process. The physical governing equations are solved by the finite volume method on a non-staggered grid and the interpolation technique on the collocated grid is used for the pressure-velocity and the stress-velocity decoupling problems. The level set and its reinitialization equation are solved by the finite difference method, in which the spatial derivatives are discretized by the 5th-order Weighted Essentially Non-Oscillatory (WENO) scheme, and the temporal derivatives are discretized by the 3rd-order Total Variation Diminishing Runge–Kutta (TVD-R–K) scheme. The validity of the method is verified by some benchmark problems. Then a simulation of viscoelastic fluid mold filling process is pursued with the method. The moving interface and all the information of the physical quantities during the injection process are captured. The die swelling phenomenon is found in the simulation. The influences of elasticity and viscosity on the physical quantities such as stresses etc. in the mold filling process are analyzed. Numerical results show that elastic characteristics such as the stretch and die swelling etc. reinforce accordingly as Weissenberg number increases. Pressures increase continuously in the mold filling process and the pressure maintains the maximum value at the inlet. Injection velocity is proportional to injection pressure. A higher viscosity leads to a higher pressure distribution, that is, the pressure decreases as Reynolds number increases.</description><identifier>ISSN: 0377-0257</identifier><identifier>EISSN: 1873-2631</identifier><identifier>DOI: 10.1016/j.jnnfm.2010.06.011</identifier><identifier>CODEN: JNFMDI</identifier><language>eng</language><publisher>Oxford: Elsevier B.V</publisher><subject>Applied sciences ; Computer simulation ; Derivatives ; Exact sciences and technology ; Gas–liquid flow ; Level set ; Machinery and processing ; Mathematical analysis ; Mathematical models ; Mold filling ; Molds ; Moulding ; Navier-Stokes equations ; Plastics ; Polymer ; Polymer industry, paints, wood ; Technology of polymers ; Viscoelastic fluid ; Viscoelastic fluids ; Viscosity</subject><ispartof>Journal of non-Newtonian fluid mechanics, 2010-10, Vol.165 (19), p.1275-1293</ispartof><rights>2010 Elsevier B.V.</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c365t-c2bff88ab510700e6acd962d55e540497d2d3602451326f8b3b39e9685ee0f0b3</citedby><cites>FETCH-LOGICAL-c365t-c2bff88ab510700e6acd962d55e540497d2d3602451326f8b3b39e9685ee0f0b3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=23303243$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Yang, Binxin</creatorcontrib><creatorcontrib>Ouyang, Jie</creatorcontrib><creatorcontrib>Li, Qiang</creatorcontrib><creatorcontrib>Zhao, Zhifeng</creatorcontrib><creatorcontrib>Liu, Chuntai</creatorcontrib><title>Modeling and simulation of the viscoelastic fluid mold filling process by level set method</title><title>Journal of non-Newtonian fluid mechanics</title><description>A model for unifying a viscoelastic fluid and a Newtonian fluid is established, in which the governing equations for the viscoelastic fluid and the Newtonian fluid are successfully united into a system of generalized Navier–Stokes equations. A level set method is set up to solve the model for capturing the moving interface in the mold filling process. The physical governing equations are solved by the finite volume method on a non-staggered grid and the interpolation technique on the collocated grid is used for the pressure-velocity and the stress-velocity decoupling problems. The level set and its reinitialization equation are solved by the finite difference method, in which the spatial derivatives are discretized by the 5th-order Weighted Essentially Non-Oscillatory (WENO) scheme, and the temporal derivatives are discretized by the 3rd-order Total Variation Diminishing Runge–Kutta (TVD-R–K) scheme. The validity of the method is verified by some benchmark problems. Then a simulation of viscoelastic fluid mold filling process is pursued with the method. The moving interface and all the information of the physical quantities during the injection process are captured. The die swelling phenomenon is found in the simulation. The influences of elasticity and viscosity on the physical quantities such as stresses etc. in the mold filling process are analyzed. Numerical results show that elastic characteristics such as the stretch and die swelling etc. reinforce accordingly as Weissenberg number increases. Pressures increase continuously in the mold filling process and the pressure maintains the maximum value at the inlet. Injection velocity is proportional to injection pressure. A higher viscosity leads to a higher pressure distribution, that is, the pressure decreases as Reynolds number increases.</description><subject>Applied sciences</subject><subject>Computer simulation</subject><subject>Derivatives</subject><subject>Exact sciences and technology</subject><subject>Gas–liquid flow</subject><subject>Level set</subject><subject>Machinery and processing</subject><subject>Mathematical analysis</subject><subject>Mathematical models</subject><subject>Mold filling</subject><subject>Molds</subject><subject>Moulding</subject><subject>Navier-Stokes equations</subject><subject>Plastics</subject><subject>Polymer</subject><subject>Polymer industry, paints, wood</subject><subject>Technology of polymers</subject><subject>Viscoelastic fluid</subject><subject>Viscoelastic fluids</subject><subject>Viscosity</subject><issn>0377-0257</issn><issn>1873-2631</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2010</creationdate><recordtype>article</recordtype><recordid>eNp9kEFP4zAQha3VIm238Av24gvilDK2Yyc5cFghdkEq4gIXLpZjjxdXTszGaaX-e0yLODKXkUbfm3nzCPnFYMWAqcvNajOOflhxKBNQK2DsG1mwthEVV4J9JwsQTVMBl80P8jPnDZSSQi3I831yGMP4j5rR0RyGbTRzSCNNns4vSHch24TR5DlY6uM2ODqk6KgP8aB6nZLFnGm_pxF3GGnGmQ44vyR3Sk68iRnPPvqSPP25eby-rdYPf--uf68rK5ScK8t779vW9JJBA4DKWNcp7qREWUPdNY47oYDXkgmufNuLXnTYqVYigodeLMnFcW_x8n-LedZDMY0xmhHTNutW1TXratYWUhxJO6WcJ_T6dQqDmfaagX4PUm_0IUj9HqQGpUuQRXX-sd9ka6KfzGhD_pRyIUDwWhTu6shheXYXcNLZBhwtujChnbVL4cs7b65bilE</recordid><startdate>20101001</startdate><enddate>20101001</enddate><creator>Yang, Binxin</creator><creator>Ouyang, Jie</creator><creator>Li, Qiang</creator><creator>Zhao, Zhifeng</creator><creator>Liu, Chuntai</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>7U5</scope><scope>8FD</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>20101001</creationdate><title>Modeling and simulation of the viscoelastic fluid mold filling process by level set method</title><author>Yang, Binxin ; Ouyang, Jie ; Li, Qiang ; Zhao, Zhifeng ; Liu, Chuntai</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c365t-c2bff88ab510700e6acd962d55e540497d2d3602451326f8b3b39e9685ee0f0b3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2010</creationdate><topic>Applied sciences</topic><topic>Computer simulation</topic><topic>Derivatives</topic><topic>Exact sciences and technology</topic><topic>Gas–liquid flow</topic><topic>Level set</topic><topic>Machinery and processing</topic><topic>Mathematical analysis</topic><topic>Mathematical models</topic><topic>Mold filling</topic><topic>Molds</topic><topic>Moulding</topic><topic>Navier-Stokes equations</topic><topic>Plastics</topic><topic>Polymer</topic><topic>Polymer industry, paints, wood</topic><topic>Technology of polymers</topic><topic>Viscoelastic fluid</topic><topic>Viscoelastic fluids</topic><topic>Viscosity</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Yang, Binxin</creatorcontrib><creatorcontrib>Ouyang, Jie</creatorcontrib><creatorcontrib>Li, Qiang</creatorcontrib><creatorcontrib>Zhao, Zhifeng</creatorcontrib><creatorcontrib>Liu, Chuntai</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical &amp; Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Journal of non-Newtonian fluid mechanics</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Yang, Binxin</au><au>Ouyang, Jie</au><au>Li, Qiang</au><au>Zhao, Zhifeng</au><au>Liu, Chuntai</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Modeling and simulation of the viscoelastic fluid mold filling process by level set method</atitle><jtitle>Journal of non-Newtonian fluid mechanics</jtitle><date>2010-10-01</date><risdate>2010</risdate><volume>165</volume><issue>19</issue><spage>1275</spage><epage>1293</epage><pages>1275-1293</pages><issn>0377-0257</issn><eissn>1873-2631</eissn><coden>JNFMDI</coden><abstract>A model for unifying a viscoelastic fluid and a Newtonian fluid is established, in which the governing equations for the viscoelastic fluid and the Newtonian fluid are successfully united into a system of generalized Navier–Stokes equations. A level set method is set up to solve the model for capturing the moving interface in the mold filling process. The physical governing equations are solved by the finite volume method on a non-staggered grid and the interpolation technique on the collocated grid is used for the pressure-velocity and the stress-velocity decoupling problems. The level set and its reinitialization equation are solved by the finite difference method, in which the spatial derivatives are discretized by the 5th-order Weighted Essentially Non-Oscillatory (WENO) scheme, and the temporal derivatives are discretized by the 3rd-order Total Variation Diminishing Runge–Kutta (TVD-R–K) scheme. The validity of the method is verified by some benchmark problems. Then a simulation of viscoelastic fluid mold filling process is pursued with the method. The moving interface and all the information of the physical quantities during the injection process are captured. The die swelling phenomenon is found in the simulation. The influences of elasticity and viscosity on the physical quantities such as stresses etc. in the mold filling process are analyzed. Numerical results show that elastic characteristics such as the stretch and die swelling etc. reinforce accordingly as Weissenberg number increases. Pressures increase continuously in the mold filling process and the pressure maintains the maximum value at the inlet. Injection velocity is proportional to injection pressure. A higher viscosity leads to a higher pressure distribution, that is, the pressure decreases as Reynolds number increases.</abstract><cop>Oxford</cop><pub>Elsevier B.V</pub><doi>10.1016/j.jnnfm.2010.06.011</doi><tpages>19</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0377-0257
ispartof Journal of non-Newtonian fluid mechanics, 2010-10, Vol.165 (19), p.1275-1293
issn 0377-0257
1873-2631
language eng
recordid cdi_proquest_miscellaneous_864419418
source ScienceDirect Freedom Collection
subjects Applied sciences
Computer simulation
Derivatives
Exact sciences and technology
Gas–liquid flow
Level set
Machinery and processing
Mathematical analysis
Mathematical models
Mold filling
Molds
Moulding
Navier-Stokes equations
Plastics
Polymer
Polymer industry, paints, wood
Technology of polymers
Viscoelastic fluid
Viscoelastic fluids
Viscosity
title Modeling and simulation of the viscoelastic fluid mold filling process by level set method
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-28T11%3A54%3A48IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Modeling%20and%20simulation%20of%20the%20viscoelastic%20fluid%20mold%20filling%20process%20by%20level%20set%20method&rft.jtitle=Journal%20of%20non-Newtonian%20fluid%20mechanics&rft.au=Yang,%20Binxin&rft.date=2010-10-01&rft.volume=165&rft.issue=19&rft.spage=1275&rft.epage=1293&rft.pages=1275-1293&rft.issn=0377-0257&rft.eissn=1873-2631&rft.coden=JNFMDI&rft_id=info:doi/10.1016/j.jnnfm.2010.06.011&rft_dat=%3Cproquest_cross%3E864419418%3C/proquest_cross%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c365t-c2bff88ab510700e6acd962d55e540497d2d3602451326f8b3b39e9685ee0f0b3%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=864419418&rft_id=info:pmid/&rfr_iscdi=true