Abstract
Particle suspension is an important parameter in the design of an energy-efficient Pachuca tank. Unfortunately, very little attention has been focused on the suspension behavior of air-agitated Pachucas. In the present investigation, therefore, extensive experiments have been carried out in three laboratory-scale Pachuca tanks to examine the effect of design and operating parameters, as well as scale-up, on particle suspension. A mathematical model that combines the Bernoulli’s equation and the theory of transport of particles in the horizontal flow of a liquid has been developed to predict the critical gas velocity for particle suspension in Pachuca tanks. Some important results, crucial to the design and scale-up of Pachuca tanks, have emerged. Full-center-column (FCC) Pachuca tanks with a draft tube-to-tank diameter ratio (D d/Dt) on the order of 0.1 are found to be energetically more efficient in suspending particles than free-air-lift (FAL) and stub-column (SC) Pachuca tanks. It is also observed that taller tanks require lower air flow rates for particle suspension than shallower tanks. Finally, it is explained why industrial Pachuca tanks operate at lower air velocities than laboratory-scale tanks.
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Abbreviations
- A :
-
cross-sectional area (m2)
- D :
-
diameter (m)
- f :
-
friction factor averaged over a rough flat surface (—)
- H :
-
height (m)
- K :
-
empirical factor defined by Eq. [17] (—)
- K fd :
-
frictional energy loss coefficient in the draft tube (—)
- K ru :
-
energy loss coefficient due to flow reversal and sudden expansion at the top of the tank (—)
- K rl :
-
energy loss coefficient due to flow reversal and sudden contraction at the bottom of the tank (—)
- K s :
-
sand equivalent roughness (m)
- n 1 through n 4 :
-
constants defined by Eq. [16] (—)
- Re p :
-
particle Reynolds number (ρ lU∞dp/μl)
- U c :
-
critical superficial air velocity for particle suspension (m s−1)
- U ∞ :
-
terminal velocity of a particle in a stagnant liquid (m s−1)
- U gd :
-
superficial air velocity in the draft tube (m s−1)
- U ld :
-
superficial liquid velocity in the draft tube (m s−1)
- U la :
-
superficial liquid velocity in the annulus (m s−1)
- U lf :
-
mean liquid velocity over a flat plate (m s−1)
- U l,c :
-
critical mean liquid velocity at the cone (m s−1)
- u*:
-
friction velocity (m s−1)
- V ld :
-
absolute liquid velocity in the draft tube (m s−1)
- v*:
-
root-mean-square of vertical velocity component of turbulent eddies
- FAL:
-
free-air-lift Pachuca tank
- FCC:
-
full-center-column Pachuca tank
- SC:
-
stub-column Pachuca tank
- α :
-
turbulence damping coefficient, defined by Eq. [3]
- φ :
-
gas holdup
- ɛ :
-
volume fraction of solid
- ρ :
-
density (kg m−3)
- μ :
-
viscosity (kg m−1 s−1)
- τ 2 :
-
wall shear stress (kg m−1 s−1)
- a :
-
annulus
- b :
-
bottom
- c :
-
cone
- d :
-
draft tube
- g :
-
gas
- l :
-
liquid
- t :
-
tank
- w :
-
wall
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Roy, G.G., Shekhar, R. & Mehrotra, S.P. Particle suspension in (air-agitated) pachuca tanks. Metall Mater Trans B 29, 339–349 (1998). https://doi.org/10.1007/s11663-998-0111-1
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DOI: https://doi.org/10.1007/s11663-998-0111-1