1998
DOI: 10.1017/s0022112098002651
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Modelling of concentrated suspensions using a continuum constitutive equation

Abstract: We simulate the behaviour of suspensions of large-particle, non-Brownian, neutrally-buoyant spheres in a Newtonian liquid with a Galerkin, finite element, Navier–Stokes solver into which is incorporated a continuum constitutive relationship described by Phillips et al. (1992). This constitutive description couples a Newtonian stress/shear-rate relationship (where the local viscosity of the suspension is dependent on the local volume fraction of solids) with a shear-induced migration model of the sus… Show more

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Cited by 84 publications
(69 citation statements)
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References 37 publications
(71 reference statements)
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“…The solid fraction decreases in front of the piston pushing the suspension and is higher in the second half of the domain along the pipe axis. This is in agreement with experimental observation [9]. The mean solid fraction on sections normal to the pipe axis was computed and plotted along the pipe axis in Figure 9.…”
Section: Piston-driven Flowsupporting
confidence: 89%
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“…The solid fraction decreases in front of the piston pushing the suspension and is higher in the second half of the domain along the pipe axis. This is in agreement with experimental observation [9]. The mean solid fraction on sections normal to the pipe axis was computed and plotted along the pipe axis in Figure 9.…”
Section: Piston-driven Flowsupporting
confidence: 89%
“…The uniformity of the suspension downstream of the piston will then affect the distribution of particles inside the molded part. An experimental study of this problem was performed by Subia et al [9]. The piston radius is 2.54 cm and the pipe was filled with material on a length of 30 cm.…”
Section: Piston-driven Flowmentioning
confidence: 99%
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“…The used benchmark corresponds to the pipe flow studied in [43]: it consists of a pressure-driven axial flow of a monomodal suspension through a 122 cm long pipe with radius 2.54 cm. A uniformly mixed suspension of spherical particles of 3178 mm in diameter with initial volume fraction of 0.50 was set in motion under an inlet mass flow rate of 0.3 kg s 21 with a constant inlet volume fraction of 0.5.…”
Section: Model Validationmentioning
confidence: 99%