1991
DOI: 10.1080/02533839.1991.9677362
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A constitutive approach for studying concentrated suspensions of rigid fibers in a non ‐ Newtonian Ellis fluid

Abstract: A constitutive model for a semi-concentrated suspension of rigid fibers in a non-Newtonian fluid is derived in the present study. This work is extended from a previous work by Dinh and Armstrong which counted rigid fibers suspended in a Newtonian fluid. To investigate the effect of the sheardependent suspending fluid on the shear viscosity of suspension, the Ellis fluid is assumed to model such a non-linear matrix. It is shown that the present derivation, via a cell model, gives an analytic form to calculate t… Show more

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Cited by 3 publications
(2 citation statements)
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“…Dinh & Armstrong (1984) also used the Batchelor approach to develop a rheological equation of state to describe non-dilute suspensions of fibres in Newtonian solvents undergoing homogeneous extensional and shear flows. This work was then extended by Wang & Cheau (1991) who proposed a constitutive model for semi-concentrated suspensions of rigid fibres in an Ellis fluid. However, in their model derivation, it was assumed that the outer boundary condition for the axial velocity isγ D/2 (γ and D/2 being respectively the shear rate and particle radius), which appears to be unphysical.…”
mentioning
confidence: 99%
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“…Dinh & Armstrong (1984) also used the Batchelor approach to develop a rheological equation of state to describe non-dilute suspensions of fibres in Newtonian solvents undergoing homogeneous extensional and shear flows. This work was then extended by Wang & Cheau (1991) who proposed a constitutive model for semi-concentrated suspensions of rigid fibres in an Ellis fluid. However, in their model derivation, it was assumed that the outer boundary condition for the axial velocity isγ D/2 (γ and D/2 being respectively the shear rate and particle radius), which appears to be unphysical.…”
mentioning
confidence: 99%
“…However, in their model derivation, it was assumed that the outer boundary condition for the axial velocity isγ D/2 (γ and D/2 being respectively the shear rate and particle radius), which appears to be unphysical. In addition, Wang & Cheau (1991) did not take into account the dependency of particle orientation on the axial velocity. Souloumiac & Vincent (1998) improved the original work of Batchelor (1971) and Goddard (1976a) by considering rod orientation and their result is applicable to homogeneous flow, especially to shear flow.…”
mentioning
confidence: 99%