Transient polymeric drop extension and retraction in uniaxial extensional flows

被引:49
作者
Hooper, RW
de Almeida, VF
Macosko, CW
Derby, JJ
机构
[1] Univ Minnesota, Minnesota Supercomp Inst, Army HPC Res Ctr, Dept Chem Engn & Mat Sci, Minneapolis, MN 55455 USA
[2] Oak Ridge Natl Lab, Div Chem Technol, Oak Ridge, TN 37831 USA
关键词
elasticity; viscoelastic fluid; boundary element method;
D O I
10.1016/S0377-0257(01)00112-4
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
We present results from modeling the deformation of a viscoelastic drop suspended in another viscoelastic fluid subjected to uniaxial extensional flow using the DEVSSG-FEM. Viscoelasticity is implemented using the Oldroyd-B constitutive relation for both the drop and surrounding matrix fluids. To allow efficient solution of the discretized problem, we employ an implicit temporal integration scheme with an accelerated quasi-Newton method. Important viscoelastic effects for both drop deformation during extensional flow and drop retraction following cessation of flow are elucidated. Viscoelastic drops in a Newtonian matrix lengthen less at steady state extension than Newtonian drops because of the accommodation of stress by elasticity. However, the stored elastic effects cause rapid tip retraction during the recovery of polymeric drops, Drops stretched in a viscoelastic exterior flow are enhanced in length compared to those in a Newtonian matrix because of first normal stresses from the matrix. During recovery, drops in a viscoelastic matrix can exhibit significant lengthening upon cessation of extensional flows, causing additional strain before retraction, This behavior is strongly dependent on the details of the exterior flow. (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:141 / 168
页数:28
相关论文
共 35 条
[1]  
Baaijens FPT, 1998, J NON-NEWTON FLUID, V79, P361, DOI 10.1016/S0377-0257(98)00122-0
[2]  
Bird R. B., 1977, Dynamics of Polymeric Liquids, V1
[3]  
Bird RB, 1987, DYNAMICS POLYM LIQUI
[4]   TRANSIENT DEFORMATION OF AN INVISCID INCLUSION IN A VISCOELASTIC EXTENSIONAL FLOW [J].
BOUSFIELD, DW ;
KEUNINGS, R ;
DENN, MM .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 1988, 27 (02) :205-221
[5]   STREAMLINE UPWIND PETROV-GALERKIN FORMULATIONS FOR CONVECTION DOMINATED FLOWS WITH PARTICULAR EMPHASIS ON THE INCOMPRESSIBLE NAVIER-STOKES EQUATIONS [J].
BROOKS, AN ;
HUGHES, TJR .
COMPUTER METHODS IN APPLIED MECHANICS AND ENGINEERING, 1982, 32 (1-3) :199-259
[6]  
DEALMEIDA VF, 1999, NUM METH PARTIAL DIF, V16, P11
[7]  
DEALMEIDA VF, 1999, IN PRESS SIAM J SCI
[8]   Droplet deformation in immiscible polymer blends during transient uniaxial elongational flow [J].
Delaby, I ;
Ernst, B ;
Froelich, D ;
Muller, R .
POLYMER ENGINEERING AND SCIENCE, 1996, 36 (12) :1627-1635
[9]   Drop deformation during elongational flow in blends of viscoelastic fluids. Small deformation theory and comparison with experimental results [J].
Delaby, I ;
Ernst, B ;
Muller, R .
RHEOLOGICA ACTA, 1995, 34 (06) :525-533
[10]   DROPLET DEFORMATION IN POLYMER BLENDS DURING UNIAXIAL ELONGATIONAL FLOW - INFLUENCE OF VISCOSITY RATIO FOR LARGE CAPILLARY NUMBERS [J].
DELABY, I ;
ERNST, B ;
GERMAIN, Y ;
MULLER, R .
JOURNAL OF RHEOLOGY, 1994, 38 (06) :1705-1720