2012
DOI: 10.1002/app.36648
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Simulations of a full three‐dimensional packing process and flow‐induced stresses in injection molding

Abstract: Numerical investigations of a full threedimensional (3D) packing process and flow-induced stresses are presented. The model was constructed on the basis of a 3D nonisothermal weakly compressible viscoelastic flow model combined with extended pom-pom (XPP) constitutive and Tait state equations. A hybrid finite element method (FEM)-finite volume method (FVM) is proposed for solving this model. The momentum equations were solved by the FEM, in which a discrete elastic viscous stress split scheme was used to overc… Show more

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Cited by 9 publications
(13 citation statements)
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“…The numerical simulation of the above model employs hybrid FEM/FVM [18] method. The momentum equations are solved by the FEM, in which a discrete elastic viscous stress split (DEVSS) scheme is used to overcome the elastic stress instability, and an implicit scheme of iterative weaklycompressible Crank-Nicolson-based split scheme (WCNBS) is used to avoid the Ladyzhenskaya-Babuška-Brezzi (LBB) condition.…”
Section: Methodsmentioning
confidence: 99%
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“…The numerical simulation of the above model employs hybrid FEM/FVM [18] method. The momentum equations are solved by the FEM, in which a discrete elastic viscous stress split (DEVSS) scheme is used to overcome the elastic stress instability, and an implicit scheme of iterative weaklycompressible Crank-Nicolson-based split scheme (WCNBS) is used to avoid the Ladyzhenskaya-Babuška-Brezzi (LBB) condition.…”
Section: Methodsmentioning
confidence: 99%
“…Tait state equation [18] is usually considered as the classical empirical equation and is capable of describing both the liquid and solid regions. So Tait state equation is used in this paper.…”
Section: Governing Equationsmentioning
confidence: 99%
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“…Thus, the polymer melt near the mould wall will cool and solidify quickly. In order to describe the change of viscoelastic melt with the temperature and pressure, we adopt the double domain Tait state equation to describe the melt density change: 1ρm=V0true(Ttrue)true[1C0Intrue(1+pBtrue(Ttrue)true)true]+Vttrue(p,Ttrue) where V0true(Ttrue)=true{leftcenterb1,m+b2,mtrue(Tb5true) if T>Ttcenterb1,s+b2,strue(Tb5true) if T<Tt; Btrue(Ttrue)=true{leftcenterβ3,mexptrue[b4,mtrue(Tb5true)true] if T>TtcenterB3,sexptrue[b4,strue(Tb5true)true] if T<Tt; and ...…”
Section: Gas‐liquid Two‐phase Modelmentioning
confidence: 99%
“…This fact has motivated the work of some researchers on computational rheology, and important insights have been obtained over the years. In particular, for the XPP model we highlight the following works: Yang et al [37] simulated the mold filling process combining a level set method and the finite volume method on a non-staggered grid; Jiang et al [38] studied the impact of liquid droplets on solid surfaces using an improved Smoothed Particle Hydrodynamics method; Qiang et al [39] analysed the gas-assisted injection molding process using Level Set/SIMPLEC methods; more recently, Li et al [40] simulated the full three-dimensional packing process in injection molding.…”
Section: Introductionmentioning
confidence: 99%