Hydrodynamic stability of unidirectional shear flow of linear and branched polymeric melts

被引:2
作者
Arora, K [1 ]
Ganesan, V [1 ]
Sureshkumar, R [1 ]
Khomami, B [1 ]
机构
[1] Washington Univ, Dept Chem Engn, Mat Res Lab, St Louis, MO 63130 USA
基金
美国国家科学基金会;
关键词
polymeric melts; pompom model; stability analysis; eigenspectrum; dynamic simulations;
D O I
10.1016/j.jnnfm.2004.06.001
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
In this study, the linear stability of homogeneous shear flow of polymer melts has been investigated by using a prototypical reptation-based model, namely, the Pompom model [1]. The hydrodynamic stability characteristics of the flow have been determined by using an eigenvalue analysis. Particular attention has been paid to accurate determination of the discrete and continuous eigenvalues as well as identification and isolation of the spurious eigenvalues. Specifically, it has been shown that the eigenspectrum for the Pompom model has four continuous spectra, three of which are associated with the orientation tensor, S, i.e., one regular and two branch-cuts. One spectrum arises as a result of the stretch, X evolution equation, which always occurs as the leftmost spectrum. The discrete modes are classified as centered and non-centered eigenvalues, depending on their imaginary parts. It is shown that there is only one pair of non-centered eigenvalues (a non-centered eigenvalue possesses sigma(i) not equal sigma/2, where sigma(i) denotes the imaginary part of the eigenvalue and alpha denotes the wavenumber in the streamwise direction). For large deformations rates, the real parts of these eigenvalues decay in a similar fashion as the Gorodstov-Leonov eigenvalue pair [2], observed in planar flows of the Upper Convected Maxwell model (UCM). The number of centered eigenvalues however, depends strongly on the choice of parameters. We observe that the leading eigenvalues always belong to the right-most continuous mode (branch-cut), which possess highly singular eigenfunctions. Although, the flow is linearly stable when a maximum in the shear stress versus shear rate curve is not observed, the ballooning of the right most eigenspectrum that arises due to the singular nature of its eigenfunctions could lead to erroneous determination of onset conditions for the instability. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:101 / 115
页数:15
相关论文
共 22 条
[1]   Influence of energetics on the stability of viscoelastic Taylor-Couette flow [J].
Al-Mubaiyedh, UA ;
Sureshkumar, R ;
Khomami, B .
PHYSICS OF FLUIDS, 1999, 11 (11) :3217-3226
[2]   Linear stability of viscoelastic Taylor-Couette flow: Influence of fluid rheology and energetics [J].
Al-Mubaiyedh, UA ;
Sureshkumar, R ;
Khomami, B .
JOURNAL OF RHEOLOGY, 2000, 44 (05) :1121-1138
[3]   Molecular drag-strain coupling in branched polymer melts [J].
Blackwell, RJ ;
McLeish, TCB ;
Harlen, OG .
JOURNAL OF RHEOLOGY, 2000, 44 (01) :121-136
[4]   Stability analysis of polymer shear flows using the eXtended Pom-Pom constitutive equations [J].
Bogaerds, ACB ;
Grillet, AM ;
Peters, GWM ;
Baaijens, FPT .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2002, 108 (1-3) :187-208
[5]  
CANUTO C, 1988, SPECTRAL METHODS FLU, pCH3
[6]  
DAVID SM, 1990, J COMPUT PHYS, V87, P464
[7]  
De Gennes PG., 1979, SCALING CONCEPTS POL
[8]  
GORODTSOV VA, 1967, J APPL MATH MECH-USS, V31, P310
[9]   Effect of axial flow on viscoelastic Taylor-Couette instability [J].
Graham, MD .
JOURNAL OF FLUID MECHANICS, 1998, 360 :341-374
[10]   Stability analysis of constitutive equations for polymer melts in viscometric flows [J].
Grillet, AM ;
Bogaerds, ACB ;
Peters, GWM ;
Baaijens, FPT .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2002, 103 (2-3) :221-250