Simulation of linear polymer melts in transient complex flow

被引:27
作者
Wapperom, P [1 ]
Keunings, R [1 ]
机构
[1] Univ Catholique Louvain, Div Appl Mech, CESAME, B-1348 Louvain, Belgium
基金
澳大利亚研究理事会;
关键词
Lagrangian particle methods; deformation field method; integral models; reptation; contraction/expansion;
D O I
10.1016/S0377-0257(00)00165-8
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Recently, much progress has been made in improving the modelling of linear polymer melts with the aid of reptation theory. In simple shear flows, this has resulted in a much better prediction of the shear viscosity and normal stress ratio. Here, we evaluate in complex flow the transient and steady-state behaviour of a recently proposed reptation model, the Marrucci-Greco-Ianniruberto model [G. Marrucci, F Greco, G. Ianniruberto, Rheol. Acta, 2000, submitted for publication], that includes convective constraint release and a force balance on the entanglement nodes. To incorporate integral type models into the numerical framework of Lagrangian particle methods, developed previously to simulate dilute polymer solutions, we have included the so-called deformation field method. For the contraction/expansion flow that we consider, we find that a correction of the convective constraint release contribution to the relaxation time is necessary to avoid the unphysical situation of negative relaxation times. With this correction, we could obtain mesh and time convergence for high Weissenberg numbers without adding any solvent viscosity. We find that in complex flow also, both the steady-state and transient response of the integral model can be very well approximated by a constitutive equation of differential type. Due to the dominance of the strong thinning in both shear and elongational flows for the model, however, the inelastic Carreau-Yasuda model reproduces the steady-state kinematics and pressure drop as well. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:67 / 83
页数:17
相关论文
共 13 条
[1]  
Bird RB, 1987, DYNAMICS POLYM LIQUI
[2]  
Doi M., 1986, The Theory of Polymer Dynamics
[3]   A NEW MIXED FINITE-ELEMENT METHOD FOR COMPUTING VISCOELASTIC FLOWS [J].
GUENETTE, R ;
FORTIN, M .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 1995, 60 (01) :27-52
[4]   The Lagrangian particle method for macroscopic and micro-macro viscoelastic flow computations [J].
Halin, P ;
Lielens, G ;
Keunings, R ;
Legat, V .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 1998, 79 (2-3) :387-403
[5]   On compatibility of the Cox-Merz rule with the model of Doi and Edwards [J].
Ianniruberto, G ;
Marrucci, G .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 1996, 65 (2-3) :241-246
[6]  
MARRUCCI G, 1988, GAZZ CHIM ITAL, V118, P179
[7]  
MARRUCCI G, IN PRESS RHEOL ACTA
[8]  
MARRUCCI G, COMMUNICATION
[9]   Molecular constitutive equations for a class of branched polymers: The pom-pom polymer [J].
McLeish, TCB ;
Larson, RG .
JOURNAL OF RHEOLOGY, 1998, 42 (01) :81-110
[10]   A molecular theory for fast flows of entangled polymers [J].
Mead, DW ;
Larson, RG ;
Doi, M .
MACROMOLECULES, 1998, 31 (22) :7895-7914