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  On the drag of freely falling non-spherical particles.

Bagheri, G., & Bonadonna, C. (2016). On the drag of freely falling non-spherical particles. Powder Technology, 301, 526-544. doi:10.1016/j.powtec.2016.06.015.

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Item Permalink: http://hdl.handle.net/11858/00-001M-0000-002B-AC2B-A Version Permalink: http://hdl.handle.net/11858/00-001M-0000-002D-1526-A
Genre: Journal Article

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 Creators:
Bagheri, Gholamhossein1, Author              
Bonadonna, C., Author
Affiliations:
1Laboratory for Fluid Dynamics, Pattern Formation and Biocomplexity, Max Planck Institute for Dynamics and Self-Organization, Max Planck Society, ou_2063287              

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Free keywords: Drag coefficient; Terminal velocity; Free fall; Particle shape; Non-spherical; Irregular
 Abstract: We present a new general model for the prediction of the drag coefficient of non-spherical solid particles of regular and irregular shapes falling in gas or liquid valid for sub-critical particle Reynolds numbers (i.e. Re<3 x 10(5)). Results are obtained from experimental measurements on 300 regular and irregular particles in the air and analytical solutions for ellipsoids. Depending on their size, irregular particles are accurately characterized with a 3D laser scanner or SEM micro-CF method. The experiments are carried out in settling columns with height of 0.45 to 3.60 m and in a 4 m-high vertical wind tunnel. In addition, 881 additional experimental data points are also considered that are compiled from the literature for particles of regular shapes falling in liquids. New correlation is based on the particle Reynolds number and two new shape descriptors defined as a function of particle flatness, elongation and diameter. New shape descriptors are easy-to-measure and can be more easily characterized than sphericity. The new correlation has an average error of similar to 10%, which is significantly lower than errors associated with existing correlations. Additional aspects of particle sedimentation are also investigated. First, it is found that particles falling in dense liquids, in particular at Re>1000, tend to fall with their maximum projection area perpendicular to their falling direction, whereas in gases their orientation is random. Second, effects of small-scale surface vesicularity and roughness on the drag:coefficient of non-spherical particles found to be <10%. Finally, the effect of particle orientation on the drag coefficient is discussed and additional correlations are presented to predict the end members of drag coefficient due to change in the particle orientation.

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Language(s): eng - English
 Dates: 2016-06-142016-11
 Publication Status: Published in print
 Pages: -
 Publishing info: -
 Table of Contents: -
 Rev. Method: Peer
 Identifiers: DOI: 10.1016/j.powtec.2016.06.015
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Title: Powder Technology
Source Genre: Journal
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Pages: - Volume / Issue: 301 Sequence Number: - Start / End Page: 526 - 544 Identifier: -