Cohesive particle mixing and segregation under shear
Hongming Li, J.J. McCarthy
⁎
Department of Chemical and Petroleum, University of Pittsburgh, Pittsburgh, Pennsylvania 15261, USA
Received 15 July 2005; received in revised form 15 December 2005; accepted 21 December 2005
Available online 31 March 2006
Abstract
Mixing and segregation is important to industries ranging from food to pharmaceuticals to ceramics. Despite the fact that there have been
significant advances recently in the understanding of both free-flowing and cohesive particles, the effects of cohesion on particulate mixing and
segregation in even the simplest devices is not well understood. In this paper, we theoretically and experimentally examine the cohesive (here,
liquid-bridge induced) mixing and segregation in an annular shear cell. We extend previous theoretical arguments for pseudo-static particle
systems to sheared beds and use our theory to develop phase diagrams that correctly predict cohesive particle mixing/segregation. Interestingly,
under certain conditions mixing is stronger for small shear rates (i.e., slower stirring) than for high shear rates (i.e., faster stirring).
© 2006 Elsevier B.V. All rights reserved.
Keywords: Granular mixing; Segregation; Cohesion; Characterization
1. Introduction
The segregation of flowing granular material is a commonly
observed phenomenon in industrial processes, and has intrigued
researchers for years. Despite recent advances in the under-
standing of both free-flowing [1–6] and cohesive [1,7,8]
particles, the effects of cohesion on particulate flows in even
the simplest devices is not well understood. One problem which
has recently gained increasing multi-disciplinary interest is the
cohesive behavior caused by interstitial liquid (i.e., wet granular
materials) [1,7–11]. While it has been long believed that
cohesion mitigates segregation, the origin of this phenomenon
has been elusive [12,13]. Nevertheless, recent work focusing on
the effect of varying saturation level on segregation have shown
a rich behavior both as a function of forcing velocity [14] and
interstitial liquid viscosity [15]. Also, at a constant moisture
level, it has been shown that pseudo-static systems can exhibit
both mixing and segregation tendencies (relative to their dry
counterparts) as particle properties, such as density, size, and
surface chemistry vary [16,17].
In this paper, we examine—both theoretically and experi-
mentally—the cohesive mixing and segregation in an annular
shear cell where the importance of collisional/shearing forces are
directly controlled. We extend previous theoretical arguments
for pseudo-static particle systems to sheared beds and develop
phase diagrams which predict particle mixing/segregation.
2. Cohesive characterization
Our theory is based on previous work on characterization
tools for mono-disperse, wet granular systems [11]. Using these
tools, we have shown that in the absence of flow the transition of
non-cohesive (free-flowing) to cohesive flow occurs roughly
when the cohesive force becomes comparable to the particle
weight; however, in the presence of flow, the localized flow
behavior (collisional forces) can significantly effect this
transition [11]. By extending these tools beyond monodispersity
we can examine which cohesive interaction is most “significant”
(i.e., between similar or dissimilar materials, see Fig. 1) so that
we may predict the impact of cohesion on mixing/segregation.
2.1. Pseudo-static systems
In previous work [16,17] on pseudo-static systems, we have
shown that the Granular Bond Number, Bo
g
, may be extended
to a binary system where particles have different sizes, densities
and/or wetting characteristics. In our terminology, a pseudo-
static system is one in which no flow-related forces (e.g., shear
forces, drag forces, etc.) are larger than the weight of individual
Powder Technology 164 (2006) 58 – 64
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Corresponding author.
E-mail address: mccarthy@granular.che.pitt.edu (J.J. McCarthy).
0032-5910/$ - see front matter © 2006 Elsevier B.V. All rights reserved.
doi:10.1016/j.powtec.2005.12.018