Abstract
The spout-fluidizing characteristics of high-carbon ferromanganese powders with different sizes and masses were studied via a plexiglass spout-fluidized bed with an inner diameter of 30 mm and a height of 1000 mm. The relationships between bed voidage and such parameters as bed height, particle size, fluidizing air velocity, and air flow were obtained. Experimental results show that the powder material with high density can be fluidized in the spout-fluidized bed where the particle size is a key factor influencing the quality of fluidization.
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Abbreviations
- ɛ :
-
Bed voidage, %
- ν L :
-
Actual volume of the fluidization bed layer
- ν S :
-
True volume of powders (the ratio of mass to true density of powders)
- U mf :
-
Critical fluidization velocity, m·s−1
- d p :
-
Average diameter of solid particles, mm
- ρ f, ρ s :
-
Density of air and high-carbon ferromanganese powders respectively, kg·m−3
- μ :
-
Dynamic viscosity of air, Pa·s
- H s :
-
Bed height, mm
- D t :
-
Inner diameter of the spout-fluidized bed, mm
- g :
-
Acceleration of gravity, m·s−2
- α :
-
Spout-fluidized factor
- d e :
-
Inlet diameter, mm
- M :
-
Mass of adding material, kg
- M l :
-
Maximum mass of fluidizing material, kg
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This work was jointly sponsored by National Natural Science Foundation of China and Baosteel Group Corporation (No.50974149).
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Chen, J., Shi, Wl., Zhao, J. et al. Cold-state spout-fluidizing characteristics of high-carbon ferromanganese powders. Int J Miner Metall Mater 18, 741–747 (2011). https://doi.org/10.1007/s12613-011-0505-y
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DOI: https://doi.org/10.1007/s12613-011-0505-y