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Journal of Rheology

Volume 49, Issue 4 (Jul-Aug 2005)


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Contents

Characterization of the viscoelastic behavior of complex fluids using
the piezoelastic axial vibrator (PAV)
Jérôme J. Crassous, Raphael Régisser, Matthias Ballauff, and Norbert Willenbacher
Rheology of a dispersion of low-molar-mass liquid crystal droplets in polydimethylsiloxane
Yong Woo Inn and Morton M. Denn
Gel formation and collapse in a dispersion of a low molar mass liquid crystal in a polymer matrix
Yong Woo Inn and Morton M. Denn
A novel “cleat” geometry for suppressing wall slip
Charles S. Nickerson and Julia A. Kornfield
Origins of concentric cylinders viscometry
Prasannarao Dontula, Christopher W. Macosko, and L. E. Scriven
Rheopexy in highly concentrated emulsions
Irina Masalova, Michael Taylor, Ellina Kharatiyan, and Alexander Ya. Malkin
Morphology development of a PS/PMMA blend during start-up of uniaxial elongational flow
F. Oosterlinck, M. Mours, H.M. Laun, and P. Moldenaers
On the gap error in parallel plate rheometry that arises from the presence of air when zeroing the gap
Georgina A. Davies and Jason R. Stokes
The link between discrete and continuous modeling of liquid foam at the level of a single bubble
B. S. Gardiner and A. Tordesillas

Characterization of the viscoelastic behavior of complex fluids using
the piezoelastic axial vibrator (PAV)

Jérôme J. Crassous, Raphael Régisser, and Matthias Ballauff
Physikalische Chemie I, University of Bayreuth, 95440 Bayreuth, Germany

Norbert Willenbacher
Polymer Research Division, BASF Aktiengesellschaft, D-67056 Ludwigshafen, Germany

Abstract

The piezoelectric axial vibrator (PAV) is a squeeze-flow rheometer working at frequencies f between 1 and 4000 Hz. It can be used to measure the storage modulus and the loss modulus G´´ of complex fluids in this frequency range. Using polymer solutions with known and G´´ it is shown that the PAV gives reliable mechanical spectra for frequencies between 1 and 4000 Hz. The measurements done with the PAV are combined with a conventional mechanical rheometer (10-3f ≤ 15 Hz) and a set of torsional resonators (f = 13, 25 and 77 kHz) to obtain and G´´ between 10-3 Hz and 77 kHz. Using this combination we present the first analysis of the viscoelasticity of an aqueous suspension of thermosensitive latex particles in this range of frequency. It is demonstrated that the combination of the three devices gives the entire mechanical spectra without resort to the time-temperature superposition principle.

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Rheology of a dispersion of low-molar-mass liquid crystal droplets in polydimethylsiloxane*

Yong Woo Inn and Morton M. Denn a)

Benjamin Levich Institute for Physico-Chemical Hydrodynamics
and Department of Chemical Engineering
City College New York, CUNY, New York, NY 10031

Abstract

We describe the linear viscoelastic response of dispersions of droplets of two biphenylcarbonitriles that exhibit both isotropic and liquid crystalline phases, 4'-pentyl-4-bipheny1carbonitrile (5CB) and 4'-octyl-4-biphenylcarbonitrile (8CB), in polydimethylsiloxane (PDMS). The Palierne emulsion model agrees well with the storage modulus data for 8CB in both isotropic and nematic phases, but the model overpredicts the magnitude of the interfacial relaxation in the 5CB dispersion, where the volume fraction of the dispersed phase required to fit the data is substantially smaller than the actual value. Similarly, the interfacial tension of 5CB against PDMS deduced from the Palierne fit shows much less temperature dependence than values measured with pendant drop tensiometry. The 8CB droplets are small, with a narrow size distribution, while the 5CB droplets are considerably larger and have a high degree of polydispersity. The basic mechanics of the Palierne theory appear to be applicable to nematic liquids, at least under conditions where the entropic elasticity is weak relative to the interfacial stress; the data suggest, however, that the theory is not applicable to smectic systems, and it needs to be used with considerable care with large droplets accompanied by a large degree of polydispersity.

a) Author to whom correspondence should be addressed; e-mail: denn@che.ccny.cuny.edu
* The editorial process for this manuscript was carried out by Editorial Board member Paula Moldenaers.

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Gel formation and collapse in a dispersion of a low molar mass liquid crystal in a polymer matrix*

Yong Woo Inn and Morton M. Denn a)

Benjamin Levich Institute for Physico-Chemical Hydrodynamics
and Department of Chemical Engineering
City College of New York, CUNY, New York, NY 10031

Abstract

A dispersion of 4'-octyl-4-biphenylcarbonitrile (8CB) in polydimethylsiloxane (PDMS) matrix exhibits a rheological response characteristic of a fractal gel when prepared at a temperature at which 8CB exists in the smectic phase. The dispersion remains gel-like throughout the smectic and nematic phases of 8CB, but collapses irreversibly to a fluid-like dispersed droplet morphology at the nematic-isotropic transition. The system appears to be kinetically trapped in one or the other morphology because of a large energy barrier between the bicontinuous gel, which is the stable morphology in the smectic regime, and the dispersed droplet, which is the stable morphology in the nematic regime; the energy barrier results from the homeotropic orientation of 8CB at the PDMS interface. The system thus provides an unusual opportunity to probe the consequences of very different length scales in the minor component in both the smectic and nematic liquid crystalline regimes. One such consequence is a controllable thousand-fold change in the storage modulus of the blend.

a) Author to whom correspondence should be addressed; e-mail: denn@ccny.cuny.edu
* The editorial process for this manuscript was carried out by Editorial Board member Paula Moldenaers.

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A novel “cleat” geometry for suppressing wall slip

Charles S. Nickerson and Julia A. Kornfield

Division of Chemistry and Chemical Engineering, California Institute of Technology
1200 E. California Blvd., Pasadena, California, USA

Abstract

We describe the use of cleated surfaces on parallel disk tools to quantitatively measure the rheological properties of diverse slip-prone fluids and soft materials. Densely-packed protrusions (0.45mm × 0.45mm cross section × 0.6mm length, 0.9mm apart) penetrate the slip layer, preventing significant flow between cleats. This creates a no-slip boundary ~0.16mm below their tips, which serves as the sample gap boundary, in direct analogy to the parallel plate geometry. This “cleat” geometry suppresses slip without application of significant normal force, it imposes well-defined shear to enable absolute measurements and is compatible with small sample volumes. The geometry is validated in steady and oscillatory shear using a series of materials not prone to slip (Newtonian oils and an entangled polymer melt). The advantage of cleated tools over other slip-prevention methods is demonstrated using increasingly challenging materials – an emulsion (mayonnaise), a suspension (peanut butter), and a biological tissue (porcine vitreous humor).

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 Origins of concentric cylinders viscometry*

Prasannarao Dontula a), Christopher W. Macosko b), and L. E. Scriven

Department of Chemical Engineering & Materials Science,
University of Minnesota, Minneapolis, MN 55455, U.S.A.

Abstract

The history of the concentric cylinders apparatus for measuring the shear viscosity of liquids, and its attribution to Maurice Couette have been explored. Examination of the Nineteenth Century literature has revealed that the concept goes back to Stokes and later Margules, the design and execution of the apparatus, apparently independently, to Perry, Couette, Mallock, and Schwedoff. Mallock's and Schwedoff's measurements were the most accurate and were within 1 % of the viscosities derived from Poiseuille's measurements, on the basis of no slip at the tube walls and cylinder surfaces. Measurement of fluid viscosity was closely linked to the adoption of the no-slip boundary condition at solid-fluid interfaces.

* This paper based on a portion of C. W. Macosko’s 2004 Bingham Medal address, 15 February 2005, Lubbock, TX.
a) Current address: Unilever Research & Development Vlaardingen, Home & Personal Care, Olivier van Noortlaan 120, 3130 AC Vlaardingen, The Netherlands.
b) To whom correspondence should be addressed. E-mail: macosko@tc.umn.edu

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Rheopexy in highly concentrated emulsions

Irina Masalova a,c), Michael Taylor b), Ellina Kharatiyan a), and Alexander Ya. Malkin a)

a) Cape Peninsula University of Technology, Faculty of Engineering, Department of Civil Engineering, PO Box 652, Cape Town 8000, Republic of South Africa

b) African Explosive Limited, Johannesburg, Republic of South Africa

Abstract

This work is describes a detailed study of the rheopectic effect in the flow of highly concentrated emulsions at low stresses. Experiments with the shear rate sweep demonstrated that the upward and downward branches of the flow curves coincide above some specific shear rate value. The upward experiments show the existence of the Newtonian part on the flow curve in the low-shear-rate domain, while the effect of yielding is observed in the downward curve. Restoration of the initial structure (and properties) after cessation of loading occurs very quickly. This allows associating the rheopexy with elastic deformations and the relaxation process (observed in frequency dependence of dynamic moduli) with characteristic times of about 0.03s. Transient processes proceed in the range of shear deformation of the order of several units. Some quantitative measures of the rheopectic behaviour are proposed and discussed. Normal stresses are constant in the low shear stress domain, but decrease sharply above the range of rheopectic behaviour. The mechanisms of the observed effects are discussed. Temperature is not an important factor in the rheopectic behaviour studied in this work.

c) Author to whom correspondence should be addressed; e-mail: masalovai@cput.ac.za

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Morphology development of a PS/PMMA blend during start-up of uniaxial elongational flow

F. Oosterlinck a), M. Mours b), H.M. Laun b), and P. Moldenaers a,c)

 a) K.U. Leuven, Department of Chemical Engineering
W. de Croylaan 46, B-3001 Leuven, Belgium

b) Polymer Research, BASF Aktiengesellschaft
D-67056 Ludwigshafen, Germany

Abstract

The morphology development of a PS/PMMA blend has been investigated during uniaxial elongational flow. For this purpose linear conservative dichroism measurements are used to gather time-resolved information and Scanning Electron Microscopy (SEM) is performed on quenched samples. With the former technique the evolution of the droplet deformation in a semi-concentrated blend is studied in real time, whereas the latter technique was used for imaging individual droplets after the elongation. It is shown that the droplet deformation is affine for the conditions under investigation and that it is possible to predict the evolution of the dichroism by existing theories and the assumption of affine deformation. It has also been verified whether rheological measurements can be used to deduce morphological information during elongational flow, as this method has been succesfully applied previously in simple shear flow.

c) Corresponding author.

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On the gap error in parallel plate rheometry that arises from the presence of air when zeroing the gap

Georgina A. Davies and Jason R. Stokes

Unilever Corporate Research
Unilever R&D Colworth
Colworth House
Sharnbrook, Bedfordshire
MK44 1LQ
United Kingdom

Abstract

When zeroing the gap between two parallel plates, the squeeze flow of air results in a detectable normal force at a finite height that is misinterpreted in rheometry as an indicator for the zero gap position. This leads to a substantial gap error using well aligned parallel plates that is accurately predicted using Stefan’s equation for squeeze flow. Minimizing or accounting for this error enables accurate rheological measurements to be performed in torsional flow using the parallel plate geometry at narrow gap heights, thus allowing shear rates of over 105 s-1 to be achieved.

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  The link between discrete and continuous modeling of liquid foam at the level of a single bubble

B. S. Gardiner a) and A. Tordesillas b,c)

a) Department of Civil and Environmental Engineering, The University of Melbourne, Australia

b) Department of Mathematics and Statistics, The University of Melbourne, Australia

Abstract

In order to test the adaptability of a novel homogenization scheme originally developed for dry granular media, a micromechanical constitutive law for three-dimensional monodisperse wet foam is developed. The advantage of the homogenization scheme is that it provides a link between the discrete bubble-scale microstructure and the continuum quantities of stress and deformation. Furthermore, the resulting constitutive law is in terms of physical material properties (e.g. fluid viscosity, surface tension, bubble radius) rather than the more phenomenological parameters like power-law indices etc. Hence, predictions of the continuum model can be, and are, compared directly to experiments and simulations. Many of the general features of foam behavior are reproduced, including small-strain elasticity, dependence on gas fraction, and Bingham plastic type deformation rate dependency. However, the current micromechanical continuum model substantially overestimates the static shear modulus and yield stress of foams in comparison to simulations and experiments. This discrepancy is due to the adoption of a mean-field assumption for the deformation in the current model. It is then argued that future micromechanical continuum models for foams cannot neglect the non-affine motions associated with bubble rearrangements. Finally, for both foams and granular materials, our study indicates that the uniform deformation assumption is only valid near the critical packing of monodisperse spherical particles.

c) Corresponding author.

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Updated 15 August 2005