2021
DOI: 10.1103/physrevfluids.6.054301
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Predicting segregation of nonspherical particles

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Cited by 10 publications
(21 citation statements)
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“…The validity of an instantaneous segregation assumption can be evaluated relative to two dimensionless parameters, the ratio of the advection timescale to the segregation timescale, Ω = SL / h 2 , and the Péclet number, which is the ratio of the advection timescale to the diffusion timescale, Pe = 2 qh / DL (Fan et al., 2014). We explore these parameters using a range of values for the length scale, 0.1 ≤ L ≤ 20 m, which represents the length of a mesh cell to ≈1/4 the flume length; the flowing layer depth, 0.2 ≤ h ≤ 0.5 m, which are the range of depths observed in channel flow; the segregation length scale 5 × 10 −5 ≤ S ≤ 2 × 10 −4 m (Jones et al., 2020, 2021; Schlick et al., 2015) for a reference particle diameter, d , of 0.25–1 mm; a 2D flow rate, 1 ≤ q = hv ≤ 5 m 2 /s; and a diffusion coefficient, 1.25 × 10 −6 ≤ D ∝ ( v / h ) d 2 ≤ 2.5 × 10 −5 m 2 /s (Fan et al., 2014). The non‐dimensional numbers then range as 2 × 10 −5 ≤ Ω ≤ 0.1 and 800 ≤ Pe ≤ 4 × 10 7 .…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…The validity of an instantaneous segregation assumption can be evaluated relative to two dimensionless parameters, the ratio of the advection timescale to the segregation timescale, Ω = SL / h 2 , and the Péclet number, which is the ratio of the advection timescale to the diffusion timescale, Pe = 2 qh / DL (Fan et al., 2014). We explore these parameters using a range of values for the length scale, 0.1 ≤ L ≤ 20 m, which represents the length of a mesh cell to ≈1/4 the flume length; the flowing layer depth, 0.2 ≤ h ≤ 0.5 m, which are the range of depths observed in channel flow; the segregation length scale 5 × 10 −5 ≤ S ≤ 2 × 10 −4 m (Jones et al., 2020, 2021; Schlick et al., 2015) for a reference particle diameter, d , of 0.25–1 mm; a 2D flow rate, 1 ≤ q = hv ≤ 5 m 2 /s; and a diffusion coefficient, 1.25 × 10 −6 ≤ D ∝ ( v / h ) d 2 ≤ 2.5 × 10 −5 m 2 /s (Fan et al., 2014). The non‐dimensional numbers then range as 2 × 10 −5 ≤ Ω ≤ 0.1 and 800 ≤ Pe ≤ 4 × 10 7 .…”
Section: Methodsmentioning
confidence: 99%
“…Importantly, the materials of two different species can have overlapping distributions of material properties, including those that lead to a segregated state (Gao et al, 2021). The rate of segregation is non-linear with concentration (Gajjar & Gray, 2014;Jones et al, 2018) and depends on the magnitude of the difference between the material properties (Jones et al, 2020(Jones et al, , 2021Schlick et al, 2015).…”
Section: Segregation Sub-modelmentioning
confidence: 99%
“…The advantage of this approach is that the sizes and densities of the two particle species need not be known in advance, and, more significantly, no analog to Figure 3 is necessary (which requires many experiments or simulations). This makes the approach applicable for particles that may vary in properties other than just size or density, such as shape 16 . Using this approach, a few simple experiments can determine the equilibrium concentration that minimizes segregation.…”
Section: Methods To Determine Equilibrium Concentrationmentioning
confidence: 99%
“…Owing to the intrinsic dissipation, external energy has to be continuously injected into granular system to keep grains in motion. Various segregation agitation methods, i.e., shear and vibration, have been used to separate and mix binary grains [13][14][15][16][17]. Many driving mechanism based on materials properties, i.e., percolation and buoyancy, have also been proposed to describe the segregation of binary mixtures [18][19][20][21][22].…”
Section: Introductionmentioning
confidence: 99%