1992
DOI: 10.1016/0892-6875(92)90007-v
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Primary and secondary fluid velocities on spiral separators

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1992
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Cited by 38 publications
(41 citation statements)
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“…The parameters used in this figure are chosen for a channel with curvature and slope that roughly correspond to a Vickers FGL commercial spiral separator (ǫ = 0.67, λ = 0.33, Holtham 1992). Streamlines of the secondary flow and contours of the axial velocity and pressure are shown.…”
Section: Velocity and Pressure Profilesmentioning
confidence: 99%
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“…The parameters used in this figure are chosen for a channel with curvature and slope that roughly correspond to a Vickers FGL commercial spiral separator (ǫ = 0.67, λ = 0.33, Holtham 1992). Streamlines of the secondary flow and contours of the axial velocity and pressure are shown.…”
Section: Velocity and Pressure Profilesmentioning
confidence: 99%
“…In experiments performed by Holtham (1992) using two commercially-available spiral separators with an approximate width of 280mm, the fluid depth was 1-12mm, an aspect ratio δ < 0.1. Thus, Stokes et al (2004Stokes et al ( , 2013 and Lee et al (2014) have exploited the small depth of the flow to develop thin-film models of particle-free and particle-laden flow in helically-wound channels.…”
Section: Introductionmentioning
confidence: 99%
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“…They have been studied in the contexts of river flow and sediment transport, [6][7][8] distillation of petroleum products, 9,10 and, of particular interest here, spiral particle separation. [11][12][13][14][15][16][17][18][19][20][21][22] Spiral particle separators are helically wound channels along which particle-laden slurries flow under gravity. They are used in the coal-and mineral-processing industries to segregate and concentrate particles of different sizes and densities.…”
Section: Introductionmentioning
confidence: 99%
“…Validating these assumptions, and experimentation in general, has proven difficult, with experimental errors in measurement of flow velocities estimated to be as high as 30%. Nevertheless, a series of experiments 11,13,14 showed that a complex secondary flow exists, that a fully-developed steady state flow profile appears relatively quickly (within 2-3 turns down the spiral), and that the fluid depth is typically very shallow (1-12mm) relative to the channel width (250-350mm). Recently, Boucher et al 15 ,16 performed experiments using positron emission particle tracking to obtain more information about the motion of particles in spiral separators, but their techniques did not allow measurement of the vertical component of the particle velocity, the free-surface shape or the bulk flow.…”
Section: Introductionmentioning
confidence: 99%