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
being the Reynolds number Re defined here as
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:
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
The match of experimental data led to the following sphericity (ø) dependent parameters:
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© 1990 Elsevier Science Publishing Co., Inc.
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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
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