Abstract
The relative motion of two spherical drops along their line of centres is considered and a general solution for creeping flow presented. The exact solution agrees with solutions previously published to certain limiting conditions and expressions for the drag force for these cases determined. Asymptotic solutions for large particle separations are also presented which may be used to predict the fractional achievement of terminal velocity of the particles.
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Abbreviations
- a :
-
characteristic diameter
- a11, a12, a21, a22:
-
constants (see (50))
- a n , b n , c n , d n :
-
constant of integration (see (8))
- A n , B n , C n , D n :
-
constant of integration=K(n)(a n , b n , c n , d n )
- A * n :
-
constant defined by (22)
- c :
-
constant=r 1 sinh α=−r 2 sinh β
- C 1/2n+1 (μ):
-
Gegenbauer polynomial of order (n+1) and degree −1/2 with argument μ
- d :
-
equivalent spherical diameter
- d L :
-
Laplace drop diameter
- E:
-
differential operator (see (5))
- E n (ξ):
-
function defined by (24)
- Fα, Fβ :
-
forces on spheres ξ=α, ξ=β respectively
- F n (ξ1, ξ2):
-
function defined by (24)
- G n (ξ):
-
function defined by (24)
- h :
-
characteristic distance in a direction parallel to flow
- h1, h2:
-
distance of centres of spheres ξ=ξ 1=α and ξ=ξ 2=β from z=0
- i :
-
subscript denoting fluid to which solution applies
- K(n):
-
= (2n-1)(2n+3)/(2n(+1)✓2c 2)
- n :
-
summation index
- p :
-
pressure
- P n (ξ), Q n (ξ):
-
functions defined by (24)
- r :
-
fluid sphere radius
- r1, r2:
-
radii of spheres ξ=ξ 1 and ξ=ξ 2 respectively
- R, Z, φ :
-
cylindrical co-ordinates
- S n (ξ):
-
function defined by (24)
- t :
-
time
- T n (ξ):
-
function defined by (24)
- U :
-
characteristic velocity
- U1, U2:
-
terminal velocities of spheres ξ=ξ 1 and ξ=ξ 2 respectively
- U f :
-
terminal settling velocity for a fluid sphere
- U n (ξ):
-
mathematical function (see (8))
- U * n (ξ):
-
function defined by (19)
- U s :
-
particle terminal settling velocity as predicted by Stokes' Law
- v :
-
vector fluid velocity
- \(\tilde V\) n (ξ):
-
=K(n) U n (ξ)
- V n (ξ):
-
function defined by (24)
- V * n (ξ):
-
=K(n) U n *(ξ)
- v R , v z , vφ:
-
velocity vector components in cylindrical co-ordinates
- v ξ , v η , vφ:
-
velocity vector components in bi-polar co-ordinates
- X :
-
=(n+1/2)α
- X n (ξ):
-
function defined by (24)
- Y :
-
=(n+1/2)β
- Y n (ξ), Z n (ξ):
-
functions defined by (24)
- α :
-
=cosh−1 (h 1/r 1)
- β :
-
=cosh−1 (h 2/r 2)
- δ :
-
constant defined by (32)
- Δ⋆, Δ ⋆1 , Δ ⋆2 , Δ ⋆33 :
-
functions defined by (24)
- ε :
-
coefficient equation (25) equals +1 when U 1=U, and −1 when U 1=−U.
- λ :
-
=λ±α, dimensionless unsteady reciprocal particle velocity =U s/U
- λ n :
-
= (λ n )±α (see (27))
- λ∞ :
-
dimensionless reciprocal terminal settling velocity for a fluid sphere =U s/U f
- λ r :
-
dimensionless reciprocal relative particle velocity =U f/U
- Γ :
-
=e−α
- μ :
-
=cos η
- μ i :
-
fluid viscosity of region i
- μ⋆:
-
dimensionless viscosity group =(3μ 1+2μ 3)(3μ 2+2μ 3)/(4(μ 1+μ 3)(μ 2+ μ 3))
- ξ, η, φ :
-
bi-polar co-ordinates
- ξ1, ξ2:
-
=α, β, respectively
- ρ :
-
density
- ν :
-
kinematic viscosity
- τξ, τηφ, τηφ :
-
components of shear stress
- σ :
-
interfacial tension
- ψ :
-
stream function
- ψ n :
-
\(\Psi = \sum\limits_{n = 0}^\infty {\Psi n} \)
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Rushton, E., Davies, G.A. The slow unsteady settling of two fluid spheres along their line of centres. Appl. Sci. Res. 28, 37–61 (1973). https://doi.org/10.1007/BF00413056
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DOI: https://doi.org/10.1007/BF00413056