Summary
The equations of motion and the mechanical energy balances for two-phase flow systems are derived by integration over a volume containing a large number of elements of the dispersed phase.
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Abbreviations
- A, A′ :
-
boundary of volumes V, V′
- dA, dA′ :
-
surface element of A, A′
- A s :
-
boundary of particles in V
- dA s :
-
surface element of A s
- F :
-
force per unit volume of the system
- g :
-
−g▽z=gravity vector
- g :
-
acceleration by gravity
- I :
-
unit tensor
- p :
-
pressure
- Q :
-
dissipation in the continuous phase
- Q s :
-
dissipation in the dispersed phase
- R :
-
compression work in the continuous phase
- R s :
-
compression work in the dispersed phase
- t :
-
time
- u :
-
velocity of continuous phase
- u s :
-
velocity of dispersed phase
- u :
-
magnitude of u
- u s :
-
magnitude of u s
- V :
-
volume in the two-phase system
- V′ :
-
part of V occupied by the continuous phase
- W :
-
work done by F
- z :
-
vertical coordinate
- α :
-
local volume fraction of the dispersed phase
- Π :
-
pI−Ψ=stress tensor of the continuous phase
- Π s :
-
turbulent particle stress tensor
- ρ :
-
density of the continuous phase
- ρ s :
-
density of the dispersed phase
- Ψ :
-
shearing-stress tensor of the continuous phase
- Ψ s :
-
turbulent particle shearing-stress tensor
- ▽ :
-
nabla operator
- ▽ u, ▽u s :
-
velocity gradient tensor
- \(\frac{D}{{Dt}} = \frac{\partial }{{\partial t}} + u \cdot \nabla \) :
-
substantial derivative
References
Leva, M., Fluidization, New York, 1959.
Santalo, M. A., Appl. Mech. Rev. 11 (1958) 523.
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(Shell Internationale Research Maatschappij N.V.)
(Bataafse Internationale Petroleum Maatschappij N.V.)
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van Deemter, J.J., van der Laan, E.T. Momentum and energy balances for dispersed two-phase flow. Appl. sci. Res. 10, 102 (1961). https://doi.org/10.1007/BF00411902
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DOI: https://doi.org/10.1007/BF00411902