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Velocity of Variously Shaped Particles Settling in Non-Newtonian Fluids

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Advances in Fine Particles Processing

Abstract

This research [1] concerns the development of a drag coefficient correlation for nonspherical particles settling in purely viscous non-Newtonian fluids. The dynamic interaction term between fluids and particles was studied using both the dimensional analysis and a large number of experimental data covering the laminar, transitional and turbulent flow regime to obtain a generalized correlation for the determination of the settling velocity valid for particles on a sphericity (ø) range from 0.5 to 1.

Unlike the previous published research in this area, this generalized correlation does not depend on a particular rheological model.

The developed correlation for the drag coefficient CD assumes the form

$${{C}_{D}}={{\left\{ {{\left[ \frac{24\Omega \left( \varnothing \right)}{{{\operatorname{Re}}_{gen}}} \right]}^{m}}+{{\left[ x\left( \varnothing \right) \right]}^{m}} \right\}}^{1/m}}$$
(1)

being the Reynolds number Re defined here as

$$\operatorname{Re}=\frac{\rho V_{t}^{2}\theta \left( \varnothing \right)}{\tau \left( \overset{\cdot }{\mathop{\gamma }}\, \right)}$$
(2)

In equation (2), θ(ø) is a known form factor and τ(\(\overset{\cdot }{\mathop{\gamma }}\,\) ) is the shear stress correspondent to a shear rate \(\overset{\cdot }{\mathop{\gamma }}\,\) related to the particle diameter dp and to the settling velocity vt by the following equation:

$$\overset{\cdot }{\mathop{\gamma }}\,=\frac{{{V}_{t}}}{{{d}_{p}}}\theta \left( \varnothing \right)$$
(3)

In equation (1) the functions Ω(ø) and X(ø) known from experiments considering the limit cases of laminar fully turbulent flow and the exponent m is determined from the data reduction using the Churchill's asymptotic method and an extensive data file from the literature.

A form for vt can be obtained by combination of the above dimension-less numbers resulting

$${{V}_{t}}={{\left\{ {{\left[ \frac{4}{3}g\frac{{{d}_{p}}\left( {{p}_{s}}-p \right)}{x\left( \varnothing \right)p} \right]}^{m}}-{{\left[ \frac{24\tau \left( \overset{\cdot }{\mathop{\gamma }}\, \right)}{\rho }\alpha \left( \varnothing \right) \right]}^{m}} \right\}}^{\frac{1}{2m}}}$$
(4)

The match of experimental data led to the following sphericity (ø) dependent parameters:

$$x\left( \varnothing \right)={{e}^{\left( 4.69-5.53\varnothing \right)}}$$
$$\alpha \left( \varnothing \right)=-\frac{\left( 1.65-0.656\varnothing \right){{e}^{\left( 5.53\varnothing -4.69 \right)}}}{\left( 3.45{{\varnothing }^{2}}-5.25\varnothing +1.41 \right)}$$
$$\Omega \left( \varnothing \right)=1.65-0.656\varnothing $$
$$\theta \left( \varnothing \right)=-3.45{{\varnothing }^{2}}+5.25\varnothing -1.41$$

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References

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Laruccia, M., Santana, C., Maidla, E. (1990). Velocity of Variously Shaped Particles Settling in Non-Newtonian Fluids. In: Hanna, J., Attia, Y.A. (eds) Advances in Fine Particles Processing. Springer, Boston, MA. https://doi.org/10.1007/978-1-4684-7959-1_8

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  • DOI: https://doi.org/10.1007/978-1-4684-7959-1_8

  • Publisher Name: Springer, Boston, MA

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