Abstract
The leaching behavior of cobalt particles in ammonia solutions has been studied. The leaching studies were carried out both in a stirred tank reactor and in a f luidized bed reactor and the results are compared with those obtained using a rotating disk geometry. Under the experimental conditions studied, the concentration difference of products between the solid /liquid interface and the bulk solution was found to be independent of the system geometry and flow dynamics. The leaching correlation obtained for cobalt particulate system was:(Sh) p = 2 + 0.65(Re) 1/2p (Sc)1/3.
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Abbreviations
- A :
-
area of leaching substrate(L2),
- Cb :
-
concentration of product in the bulk solution (mol L-3),
- C s :
-
concentration of product at the surface (mol
- d :
-
diameter of particles(L),
- D′ :
-
diameter of fluidized bed (L),
- D :
-
diffusion coefficient(L2 T− 1),
- g :
-
gravitational acceleration (MT{&x2212; 2}),
- j :
-
mass flux (ML{&x2212; 2} T{&x2212; 1}),
- k :
-
apparent rate constant (T− 1)
- k′:
-
mass transfer coefficient(LT− l),
- M :
-
moles per liter (molL− 3),
- Q :
-
volumetric flow rate (L3 T-1),
- R :
-
radius of rotating disk(L),
- V :
-
solution volume(L3),
- V p :
-
slip velocity(LT− 1),
- V t :
-
terminal velocity (LT−1),
- V fs :
-
superficial velocity of fluid(LT− 1),
- σ:
-
diffusion boundary layer thickness(L),
- ∈:
-
fractional volume of liquid in fluidized bed,
- ρ s :
-
density of solid (ML −3),
- ρf :
-
density of fluid (ML −3),
- v :
-
kinematic viscosity of fluid (L2T{−1}),
- ω:
-
angular velocity of rotating disk (radT− 1).
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Vu, C., Han, K.N. Effect of system geometry on the leaching behavior of cobalt metal: Mass transfer controlling case. Metall Trans B 10, 57–62 (1979). https://doi.org/10.1007/BF02653972
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DOI: https://doi.org/10.1007/BF02653972