Evaluation of Temperature-strain rate Dependent Uniaxial and Planar Elongational Viscosities for Branched LDPE Polymer Melt

被引:0
作者
Zatloukal, Martin [1 ]
机构
[1] Tomas Bata Univ Zlin, Fac Technol, Ctr Polymer, Zlin 76272, Czech Republic
来源
NOVEL TRENDS IN RHEOLOGY V | 2013年 / 1526卷
关键词
Orifice die; Planar elongational viscosity; Uniaxial elongational viscosity; Cogswell model; Entrance pressure drop; Polymer melts; Capillary rheometer; Constitutive equations; UNIVERSAL TESTING PLATFORM; LOW-DENSITY POLYETHYLENE; CONSTITUTIVE-EQUATIONS; FLOWS; RHEOLOGY; SHEAR; MODEL; DIE;
D O I
10.1063/1.4802613
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
In this work, novel rectangle and circular orifice dies have been utilized for temperature-strain rate dependent planar and uniaxial elongational viscosity measurements for the LDPE polymer melt by using standard twin bore capillary rheometer and Cogswell model and the capability of three different constitutive equations (novel generalized Newtonian model, modified White-Metzner model, modified Leonov model) to describe the measured experimental data has been tested. It has been shown that chain branching causes the strain hardening occurrence in both, unixial and planar elongational viscosities and its maximum is shifted to the higher strain rates if the temperature is increased. The level of uniaxial elongational strain hardening for the branched LDPE sample has been found to be higher in comparison with the planar elongational viscosity within wide range of temperatures.
引用
收藏
页码:184 / 193
页数:10
相关论文
共 29 条
[1]   A study on the flow, failure, and rupture mechanisms of low-density polyethylene in controlled-stress uniaxial extensional flow [J].
Andrade, R. J. ;
Maia, J. M. .
JOURNAL OF RHEOLOGY, 2011, 55 (05) :925-937
[2]   Cross-slot extensional rheometry and the steady-state extensional response of long chain branched polymer melts [J].
Auhl, D. ;
Hoyle, D. M. ;
Hassell, D. ;
Lord, T. D. ;
Harlen, O. G. ;
Mackley, M. R. ;
McLeish, T. C. B. .
JOURNAL OF RHEOLOGY, 2011, 55 (04) :875-900
[3]   A SIMPLE EMPIRICAL-MODEL DESCRIBING THE STEADY-STATE SHEAR AND EXTENSIONAL VISCOSITIES OF POLYMER MELTS [J].
BARNES, HA ;
ROBERTS, GP .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 1992, 44 :113-126
[4]   AN APPROXIMATE ANALYSIS FOR CONTRACTION AND CONVERGING FLOWS [J].
BINDING, DM .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 1988, 27 (02) :173-189
[5]   Response to the "Reply to: 'On the "viscosity overshoot" during the uniaxial extension of a low density polyethylene' by Rasmussen et al." [J].
Burghelea, Teodor I. ;
Stary, Zdenek ;
Munstedt, Helmut .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2012, 171 :107-108
[6]   On the "viscosity overshoot" during the uniaxial extension of a low density polyethylene [J].
Burghelea, Teodor I. ;
Stary, Zdenek ;
Muenstedt, Helmut .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2011, 166 (19-20) :1198-1209
[7]   CONVERGING FLOW OF POLYMER MELTS [J].
HUANG, DC ;
SHROFF, RN .
JOURNAL OF RHEOLOGY, 1981, 25 (06) :605-617
[8]   DIE ENTRY FLOW OF REINFORCED POLYMERS [J].
GIBSON, AG .
COMPOSITES, 1989, 20 (01) :57-64
[9]  
HACHMANN P, 1996, THESIS ETH ZURICH
[10]   Design of an orifice die to measure entrance pressure drop [J].
Kim, S ;
Dealy, JM .
JOURNAL OF RHEOLOGY, 2001, 45 (06) :1413-1419