Printer Friendly

Influence of particle shape on the viscosity of kaolin suspensions.


It is well known that particle shape has a decisive influence on suspension rheology. In particular, for kaolin suspensions, where the degree of anisometry is generally high (due to the platey shape of the kaolinite crystals), it may be expected that the effective viscosity exhibits a steeper increase with concentration than suspensions with isometric or spherical particles. A quantitative measure of the shape anisometry of particles is the aspect ratio R, which can be defined as the ratio of the longest to the shortest dimension, i.e. in the case of oblate particles (oblate spheroids, cylinderical disks or platelets) the ratio of the equatorial diameter to the height or thickness:

R = diameter / thickness. (1)

A convenient measure of the viscosity increase is the so-called "intrinsic viscosity" (or Einstein-Jeffery coefficient), which is defined as the initial slope of the relative-viscosity-versus-solids-volume-fraction curve in the dilute limit, i.e. the expression


where [phi] is the solids volume fraction and [[eta].sub.r] = [eta] / [[eta].sub.0] the relative (or reduced) viscosity, defined as the ratio of the effective viscosity of the suspension [eta] to the viscosity of the dispersing medium [[eta].sub.0]. In this work we apply a simple approximate method proposed by Pabst and Berthold (2007) to determine the average aspect ratio of three types of kaolin products (floated kaolins). The intrinsic viscosity of the corresponding kaolin suspensions is extracted from extensive viscometric measurements and compared with theoretical models available in the literature.


The first work on the rheology of anisometric particle suspensions (Jeffery, 1922) concerns ellipsoids. In Jeffery's paper an explicit analytical solution is presented, and minimum and maximum values of the intrinsic viscosity in dependence of the aspect ratio are given for (prolate and) oblate spheroids. Later work by Brenner (1974) showed that Jeffery's bounds were too wide and that the complete solution can be given in the form

[[eta]] = 5[Q.sub.1] - 15 / 4 [Q.sub.2] <[sin.sup.2] [theta]> - 5 / 4B (3[Q.sub.2] + 4[Q.sub.4]) x <[sin.sup.2] [theta]cos2[phi]> + 15 / 2BP (3[Q.sub.2] + 4[Q.sub.3]) <[sin.sup.2] [theta]sin2[phi]>, (3)

(Equation 3) where B = 5N / 3[K.sub.r] is a dimensionless parameter and P = [gamma] / [D.sub.r] the rotary Peclet number, with [gamma] being the shear rate and the rotary diffusion coefficient [D.sub.r] given by the Stokes-Einstein equation

[D.sub.r] = kT / 6V[[eta].sub.0][K.sub.r], (4)

where k is the Boltzmann constant, T the absolute temperature, V the particle volume and [[eta].sub.0] the viscosity of the suspending medium. The angular brackets denote averaging over all orientations (with polar angle [theta] and azimutal angle [phi]) and the material constants N and [K.sub.r] as well as [Q.sub.1], [Q.sub.2], [Q.sub.3], [Q.sub.4] are rather complicated functions of the aspect ratio, given in (Brenner, 1974). They are too lengthy to be written out here in explicit form. Note that Brenner's equation accounts for (rotary) Brownian motion via the rotary Peclet number (rotary diffusion coefficient). In the case of dominant Brownian motion (i.e. a very high rotary diffusion coefficient or a very low shear rate) Brenner's equation reduces to the upper bound ("zero shear rate limit")

[[[eta]].sub.0] = 5[Q.sub.1] - [Q.sub.2] + 2[Q.sub.3]. (5)

This equation (analytical solution) is in extremely good agreement with the numerical solution values obtained by Scheraga (1955) and is at the same time rather close (except for an additive constant) to the remarkably simple approximate solutions of Simha (1940) and Kuhn and Kuhn (1945), which are

[[[eta]].sub.0] = 16 / 15 R arctan([R.sup.-1]), (6)

[[[eta]].sub.0] = 4 / 9 + 32 / 15 [pi] R, (7)

respectively. Inserting into Equation 5 the explicit expressions given for [Q.sub.1], [Q.sub.2], [Q.sub.3] in Brenner's paper (Brenner, 1974), it can easily be verified that for oblate particles with aspect ratios up to 50 the linear relation [[[eta]].sub.0] [approximately equal to] 1.45 + 0.672 x R, which is the best linear fit in this range, is a reasonably precise approximation to Equation 5.


Three Czech kaolin products (floated kaolins) have been investigated in this work: KDK (Kaolin Hlubany a.s., Podborany), Imperial (Sedlecky kaolin a.s., Bozicany), SpEX (Keramika Horni Briza a.s., Kaznejov). All three are commercially available, well specified kaolin grades and are denoted by their trademark labels in this work. The particle size distributions have been measured via sedimentation in Andreasen cylinders and via laser diffraction (using the Fraunhofer approximation) on a Fritsch Particle Sizer Analysette 22 Nanotec (Fritsch Laborgeratebau GmbH, Germany). An average aspect ratio has been calculated from the difference between the two size distributions, using the relation

R = [pi] x [([D.sup.L.sub.50] / [D.sup.S.sub.50]).sup.2], (8)

where [D.sup.L.sub.50] and [D.sup.S.sub.50] are the median sizes (median equivalent sphere diameters) measured via laser diffraction and sedimentation, respectively. This relation has been derived recently (Pabst and Berthold, 2007), using a modified Stokes law for oblate spheroids and taking into account random orientation in the laser diffraction measurement via Cauchy's stereological theorem. Note that Equation 8 is an approximation for sufficiently high aspect ratios. Moreover, due to the possible (slight) dependence of the [D.sup.L.sub.50] values on the laser diffraction equipment, in particular the algorithm applied to deconvolute the diffraction pattern, absolute values must be considered with due caution. However, in spite of its deficiencies, it seems that Equation 8 represents to date the only viable route to extract an average aspect ratio of a particle system (with oblate particles). A similar relation is available for use with microscopic image analysis, see (Pabst and Berthold, 2007). The disadvantage of the latter route is that information on the average thickness of the platelets must be determined independently.

Sodium pyrophosphate (Penta a.s., Czech Republic) was used as a deflocculant for the sedimentation, laser diffraction, and rheological measurements. The optimum deflocculant content was determined individually for each kaolin by recording the flow curves of 10 wt. % kaolin suspensions with different deflocculant content, see Figure 1. It has to be emphasized that the degrees of deflocculation (and delamination) have a decisive effect on the rheological behavior of kaolin suspensions, see e.g. (Loginov et al., 2008; Moan et al., 2003; Sjoberg et al., 1999). Therefore care has been taken to perform all measurements in this paper with identically prepared suspensions.

It is evident that kaolin suspensions without deflocculant typically exhibit shear-thinning behavior whereas well deflocculated systems show a rheological behavior close to Newtonian. All suspensions were prepared by 1 h homogenization in a polyethylene bottle with alumina balls and 1 min ultrasonication (ultrasonic processor UP200S with titanium sonotrode S14, Dr. Hielscher GmbH, Germany).

Flow curves of well deflocculated kaolin suspensions with different solids contents were measured by rotational viscometry (RotoVisco 1 with concentric cylindrical sensor Z41, ThermoHaake GmbH, Germany) in the shear rate range between 0 and 1000 [s.sup.-1]. Apparent viscosities were extracted for shear rates of 200, 400, 500, 600, 800 and 1000 [s.sup.-1] and subsequently used for plotting graphs of the relative viscosity [[eta].sub.r] (using a value of 1 mPas for water at room temperature) versus the kaolin volume fraction [PHI]. The [[eta].sub.r] - [PHI] data points were finally fitted using the Krieger relation (Krieger, 1972),


in order to extract the intrinsic viscosity [[eta]] (the critical volume fraction [[PHI].sub.C] is an asymptotic value, corresponding to the maximum solids loading that the suspension may contain without loosing the ability to flow). A completely analogous procedure has been applied to isometric particles by Gregorova et al. (2006, 2008) and to prolate particles (short fiber systems) in Pabst et al. (2006). For the theoretical status of the Krieger relation, Equation 9, and its relation to other analogous power laws, the reader may consult (Pabst, 2004) and (Pabst et al., 2007).



Figure 2 (top to bottom) shows the particle size distributions of the three kaolins investigated. It is evident that the sedimentation curves are always below the laser diffraction curves. This is a common finding which may be considered of general validity, irrespective of possible equipment-specific measurement errors. From the difference of the median values we obtain via Equation 8 the average aspect ratios 17.4, 17.7 and 22.3 for kaolins KDK, Imperial and SpEX, respectively. Figure 3 (top to bottom) shows the deflocculation curves, the minimum of these curves indicating optimum deflocculation. Based on these results, deflocculant concentrations of 0.3, 0.4 and 0.6 wt. % were used for preparing the suspensions of KDK, Imperial and SpEX, respectively. Figure 4 (top to bottom) shows the flow curves of optimally deflocculated kaolin suspensions in dependence of the solids content (kaolin volume fraction). Hysteresis (indicated by error bars) is generally small and the rheological character is close to Newtonian, except at the highest concentrations.

Figure 5 (top to bottom) shows the concentration dependences of the relative viscosities, and the fit curves obtained using the Krieger relation, Equation 9. The intrinsic viscosities obtained from the fit parameters are 12.8 [+ or -] 0.4, 7.1 [+ or -] 0.2 and 6.7 [+ or -] 0.1, extrapolated values of the critical volume fraction are 0.26 [+ or -] 0.02, 0.39 [+ or -] 0.01 and 0.56 [+ or -] 0.03, for suspensions of kaolins KDK, Imperial and SpEX, respectively.

Figure 6 shows the intrinsic viscosities determined for the three kaolins in comparison to the theoretical models available in the literature.

It is evident that the data determined with the method proposed lie within the Jeffery and Brenner bounds and that an average aspect ratio of 17-22 results in an intrinsic viscosity of 7-13, compared to 2.5 for spherical particles. However, unavoidable errors of measurement (in the aspect ratio determination as well as in the viscosity measurement) do not permit to seriously assess the influence of Brownian motion. Moreover, for such a precise assessment of this kind the width of the size distribution must be taken into account. Nevertheless, the method proposed here can principally be used to predict the intrinsic viscosity when the average aspect ratio of the system (and its average size) is known, and vice versa.







Based on the investigation of three Czech kaolins as paradigmatic examples, the influence of particle shape on suspension rheology has been discussed. The Brenner relation has been identified as the currently most widely recognized model equation relating the intrinsic viscosity to the aspect ratio. A useful linear approximation to the upper bound (dominant Brownian motion) has been proposed, [[[eta]].sub.0] [approximately equal to] 1.45 + 0.672 x R, and a recently proposed formula has been used to determine an average aspect ratio from a comparison of sedimentation and laser diffraction sizing data. The intrinsic viscosity has been obtained by a multistep procedure: firstly, flow curves were recorded for each kaolin with the optimum deflocculant concentration, secondly, the (apparent) relative viscosities read off from the flow curves were plotted against the kaolin volume fraction and, thirdly, these data were fitted using the Krieger relation to obtain the intrinsic viscosity in the asymptotic dilute limit. It has been shown that the data determined with the method proposed are within the Jeffery and Brenner bounds and that an average aspect ratio of about 20 results in an intrinsic viscosity of about 10, compared to 2.5 for spherical particles.


This work was part of the research programme MSM 6046137302 "Preparation and research of functional materials and material technologies using micro- and nanoscopic methods" (Ministry of Education, Youth and Sports of the Czech Republic).


Brenner, H.: 1974, Rheology of a dilute suspension of axisymmetric Brownian particles. Int. J. Multiphase Flow, 1, 195-341.

Gregorova, E., Pabst, W. and Stetina, J.: 2006, Rheology of ceramic suspensions with biopolymeric gelling additives. Adv. Sci. Technol., 45, 462-470.

Gregorova, E., Zivcova, Z., Pabst, W., Stetina, J. and Keuper, M.: 2008, Rheology of ceramic suspensions with organic or biopolymeric gelling additives--part 3: suspensions with starch. Ceram.-Silik., 50, 250-259.

Jeffery, G.B.: 1922, The motion of ellipsoidal particles immersed in a viscous fluid. Proc. Roy. Soc. A, 102, 161-179.

Krieger, I.M.: 1972, Rheology of monodisperse latices. Adv. Colloid Interf. Sci., 3, 111-136.

Kuhn, W. and Kuhn, H.: 1945, Die Anhangigkeit der Viskositat vom Stromungsgefalle bei hochverdunnten Suspensionen und Losungen. Helv. Chim. Acta, 28, 97-127.

Loginov, M., Larue, O., Lebovka, N. and Vorobiev, E.: 2008, Fluidity of highly concentrated kaolin suspensions: Influence of particle concentration and presence of dispersant. Colloids Surf. A, 159, 197-208.

Moan, M., Aubry, T. and Bossard, F.: 2003, Nonlinear behavior of very concentrated suspensions of plate-like kaolin particles in shear flow. J. Rheol., 47, 1493-1504.

Pabst, W.: 2004, Fundamental considerations on suspension rheology. Ceram.-Silik., 48, 6-13.

Pabst, W., Gregorova, E. and Berthold, C.: 2006, Particle shape and suspension rheology of short-fiber systems. J. Eur. Ceram. Soc., 26, 149-160.

Pabst, W., Berthold, C. and Gregorova, E.: 2007, Size and shape characterization of oblate and prolate particles. J. Eur. Ceram. Soc., 27, 1759-1762.

Pabst, W. and Berthold, C.: 2007, A simple approximate formula for the aspect ratio of oblate particles. Part. Part. Syst. Charact., 24, 45 8-463.

Scheraga, H.A.: 1955, Non-Newtonian viscosity of solutions of ellipsoidal particles. J. Chem. Phys., 23, 1526-1532.

Simha, R.: 1940, The influence of Brownian movement on the viscosity of solutions. J. Phys. Chem., 44, 25-34.

Sjoberg, M., Bergstrom, L., Larsson, A. and Sjostrom, E.: 1999, The effect of polymer and surfactant adsorption on the colloidal stability and rheology of kaolin dispersions. Colloids Surf. A, 159, 197-208.

Eva GREGOROVA *, Willi PABST and Jean-Baptiste BOUCHET

Department of Glass and Ceramics, Institute of Chemical Technology, Prague (ICT Prague), Technicka 5, 166 28 Prague 6, Czech Republic

* Corresponding author's e-mail:

(Received November 2008, accepted March 2009)
COPYRIGHT 2009 Akademie Ved Ceske Republiky, Ustav Struktury a Mechaniky Hornin
No portion of this article can be reproduced without the express written permission from the copyright holder.
Copyright 2009 Gale, Cengage Learning. All rights reserved.

Article Details
Printer friendly Cite/link Email Feedback
Author:Gregorova, Eva; Pabst, Willi; Bouchet, Jean-Baptiste
Publication:Acta Geodynamica et Geromaterialia
Article Type:Report
Geographic Code:4EXCZ
Date:Jan 1, 2009
Previous Article:Prehistory of clay mineralogy--from ancient times to Agricola.
Next Article:Layered double hydroxides intercalated with organic anions and their application in preparation of LDH/polymer nanocomposites.

Terms of use | Privacy policy | Copyright © 2021 Farlex, Inc. | Feedback | For webmasters |