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A numerical study of the rheological properties of suspensions of ...

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168 M. B. Mackaplow and E. S. G. ShaqfehVolume fraction <strong>of</strong> fibres, q0 0.005 0.010 0.015 0.020 0.025Q0 2 4 6 8 10 12 14n13FIGURE 2. Normalized extra particle stress, Q, <strong>of</strong> a suspension <strong>of</strong> aligned, spheroidal fibres withaspect ratio, A = 50, as a function <strong>of</strong> <strong>the</strong> suspension volume fraction. Shown are <strong>the</strong> predictions<strong>of</strong> <strong>numerical</strong> simulations, <strong>the</strong> dilute <strong>the</strong>ory (with and without two-body corrections), and <strong>the</strong>semi-dilute <strong>the</strong>ory <strong>of</strong> Shaqfeh & Fredrickson (1990) (both <strong>the</strong> original and modified versions).ln2(2A) = 30. The ability <strong>of</strong> dilute <strong>the</strong>ories that incorporate <strong>the</strong> effects <strong>of</strong> two-bodyinteractions to predict suspension behaviour into <strong>the</strong> semi-dilute concentration regimewas also observed in our previous <strong>study</strong> <strong>of</strong> heat transfer through <strong>suspensions</strong> <strong>of</strong> highlyconducting fibres (Mackaplow et al. 1994).Figure 2 shows a plot <strong>of</strong> Q us. n13 for <strong>suspensions</strong> <strong>of</strong> fibres with an aspect ratio<strong>of</strong> 50. All <strong>of</strong> <strong>the</strong> fibres are aligned with <strong>the</strong> principal axis <strong>of</strong> extension <strong>of</strong> <strong>the</strong> flowfield. As in figure l(b), we see that by using <strong>the</strong> adjusted coefficients in <strong>the</strong> semi-dilute<strong>the</strong>ory <strong>of</strong> Shaqfeh & Fredrickson (1990), an excellent agreement between simulationsand <strong>the</strong>ory can be achieved for n13 >> 1.Figure 3 shows a plot <strong>of</strong> Q us. n13 for <strong>suspensions</strong> with a fixed inclusion volumefraction, 4, <strong>of</strong> 6.67 x . Again, <strong>the</strong>re is a positive deviation from dilute <strong>the</strong>oryfor n13 2 O( 1). Note that Q approaches a constant in <strong>the</strong> semi-dilute regime. This isconsistent with <strong>the</strong> prediction <strong>of</strong> <strong>the</strong> semi-dilute <strong>the</strong>ory that <strong>the</strong> non-dimensionalizedscreening length in a semi-dilute suspension, X/b, is only a function <strong>of</strong> <strong>the</strong> volumefraction <strong>of</strong> <strong>the</strong> suspension. Whereas <strong>the</strong> published semi-dilute <strong>the</strong>ory <strong>of</strong> Shaqfeh &Fredrickson (1990) quantitatively underestimates this value by approximately 20%,by utilizing <strong>the</strong> adjusted coefficients, excellent quantitative agreement is achieved. Asfor <strong>the</strong> previous sets <strong>of</strong> simulations, <strong>the</strong> dilute <strong>the</strong>ory with two-body corrections does agood job <strong>of</strong> predicting <strong>the</strong> suspension rheology over <strong>the</strong> entire range <strong>of</strong> concentrationsstudied.In our previous <strong>study</strong> <strong>of</strong> heat and mass transfer through fibre <strong>suspensions</strong>, similarscalings <strong>of</strong> <strong>the</strong> suspension screening length in <strong>the</strong> semi-dilute regime were observed, aspredicted by <strong>the</strong> <strong>the</strong>ory <strong>of</strong> Fredrickson & Shaqfeh (1989). However, in this previous<strong>study</strong> we found that using <strong>the</strong> <strong>the</strong>oretically predicted value <strong>of</strong> C” and neglecting <strong>the</strong>

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