Abstract
In developing a dimensionless scale-up model for small diameter hydrocyclones the influence of the particle size distribution was studied. In order to do that a batch of dolomitic limestone was divided to obtain three different grades of the same material. Suspensions with concentrations of 15% (v/v) and 20% (v/v) for each fraction of powder were tested in three geometrically similar hydrocyclones of 22mm, 44mm and 88mm in diameter. A dimensionless expression was developed to account for the particle size distribution of feed, which presented appropriate goodness of fit and showed good agreement with correlations available in the literature.
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Abbreviations
- a::
-
constant
- A::
-
settling area (L2)
- Ap::
-
projected area of particles (L2)
- b::
-
partial regression coefficient
- c::
-
feed solids concentration by volume
- CD::
-
drag coefficient
- Dc::
-
hydrocyclone body diameter (L)
- Do::
-
overflow diameter (L)
- Du::
-
underflow diameter (L)
- Eu::
-
Euler number
- FD::
-
drag force (MLT−2)
- g::
-
gravity acceleration (LT−2)
- K::
-
constant
- k1,k2::
-
constants
- kd::
-
correction factor
- kp::
-
empirical constant for a family of geometrially similar cyclones
- K′::
-
fluid consistency index (MTnL−2)
- l::
-
vortex finder length of cyclone (L)
- L::
-
overall length of cyclone body (L)
- m::
-
exponent of correction factor depending on Dc
- n::
-
flow behaviour index for power-law fluids, empirical exponent
- np::
-
empirical constant for a family of geometrically similar cyclones
- n′::
-
flow behaviour index
- Q::
-
volumetric flow rate of feed suspensions (L3T−1)
- r::
-
correlation coefficient
- R::
-
multiple correlation coefficient
- Re::
-
Reynolds number
- Re*::
-
Reynolds number for power-law fluids
- Rep*::
-
particle Reynolds number for power-law fluids
- Rf::
-
underflow-to-throughput ratio
- Stk50::
-
Stokes number
- Stk50(r)::
-
reduced Stokes number based on reduced cut size
- Stk* 50(r)::
-
reduced Stokes number for power-law fluids
- u::
-
particle-fluid relative velocity (LT−1)
- ug::
-
terminal settling velocity under gravity (LT−1)
- v::
-
superficial velocity in the cyclone body (LT−1)
- x::
-
independent variable
- x::
-
particle size (L)
- Xg::
-
mass median size (L)
- X50::
-
cut size (L)
- X50(r)::
-
reduced cut size (L)
- y::
-
dependent variable
- r::
-
viscosity coefficient for power-law fluids (ML −1Tn−2)
- i::
-
shear rate (T−1)
- ΔP::
-
pressure drop (ML−1T−2)
- μ::
-
viscosity (ML−1T−1)
- μa::
-
apparent viscosity (ML−1T−1)
- ρ::
-
liquid density (ML−3)
- ρm::
-
suspension density (ML−3)
- ρS::
-
solids density (ML−3)
- τ::
-
shear stress (ML−1T−2)
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© 1992 Springer Science+Business Media Dordrecht
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Ortega-Rivas, E., Svarovsky, L. (1992). Effect of Solids Feed Grade on the Separation of Slurries in Hydrocyclones. In: Svarovsky, L., Thew, M.T. (eds) Hydrocyclones. Fluid Mechanics and Its Applications, vol 12. Springer, Dordrecht. https://doi.org/10.1007/978-94-015-7981-0_11
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DOI: https://doi.org/10.1007/978-94-015-7981-0_11
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