1975
DOI: 10.1007/bf00862010
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Free precipitation of spherical particles in anomalous-viscosity liquids

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Cited by 1 publication
(2 citation statements)
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“…To evaluate the effect of structural parameters of the hydrocyclone (with consideration of the dimensionless flow rate Q, taper angle α of the housing, and rheologic properties of the disperse medium) on the effectiveness of separation in a hydrocyclone filtration plant, it is necessary to use integral indicators of the vessel's performance, the most important of which is the degree of extraction, which characterizes the portion of solid-phase particles extracted from the suspension in a given section of film, and which can be determined from the following formula: (13) where E = e/r k is the dimensionless height of the inlet pipe of the hydrocyclone; ∆(Z) = δ(z)/r k is the dimensionless film thickness of the suspension; θ h0 (R, Z) = v ϕh0 /u 0 is the dimensionless circumferential velocity component of solid-phase particles in the inlet pipe of the hydrocyclone; and δ(z) is the film thickness of the suspension in m.…”
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confidence: 99%
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“…To evaluate the effect of structural parameters of the hydrocyclone (with consideration of the dimensionless flow rate Q, taper angle α of the housing, and rheologic properties of the disperse medium) on the effectiveness of separation in a hydrocyclone filtration plant, it is necessary to use integral indicators of the vessel's performance, the most important of which is the degree of extraction, which characterizes the portion of solid-phase particles extracted from the suspension in a given section of film, and which can be determined from the following formula: (13) where E = e/r k is the dimensionless height of the inlet pipe of the hydrocyclone; ∆(Z) = δ(z)/r k is the dimensionless film thickness of the suspension; θ h0 (R, Z) = v ϕh0 /u 0 is the dimensionless circumferential velocity component of solid-phase particles in the inlet pipe of the hydrocyclone; and δ(z) is the film thickness of the suspension in m.…”
mentioning
confidence: 99%
“…The radial velocity component of a solid-phase particle relative to the disperse medium u rh is determined from solution of the differential equation of motion of a solid-phase particle with allowance for inertia, and the radial velocity component of a gas bubble relative to the disperse medium u rg from the formula cited in [13], disregarding the inertia of the bubble, since the density of the gas is negligible: (6) where ρ l is the density of the disperse medium in kg/m 3 ; v ϕl (r, z) is the circumferential velocity component of the disperse medium in m/sec; n is the nonlinearity indicator of the flow curve of the disperse medium; k is the consistency index of the…”
mentioning
confidence: 99%