AIChE Journal · 1987 · 47 citations · 26 references
Materials ScienceChemical EngineeringCarbon SequestrationFluid PropertiesFine Carbon PowdersEngineeringCarbonizationParticle TechnologyPowder CompactionMultiphase FlowCeramic PowdersSolidificationAbstract Particulate ExpansionChemical KineticsMinimum BubblingMinimum Bubbling ParametersPowder Synthesis
Abstract Particulate expansion and minimum bubbling parameters ( n, u ′ t , u mB , ε mB ) are measured for fine carbon powders ( d p = 44 and 112 μm) fluidized with synthesis gas (H 2 /CO = 0.8) at pressures within the range 2,070 < P < 12,420 kPa in an industrial, pilot‐scale fluidized bed. Deviations between minimum bubbling ( u mB and ε mB ) and minimum fluidization ( u mf and ε mf ) conditions increase with increasing pressure, P . The expansion index, n , decreases with increasing P and always exceeds values recommended by Richardson and Zaki for solid/liquid systems. Particulate bed expansion for the fine powders is well characterized by the equations of Foscolo et al. and Abrahamsen and Geldart. The theory of Foscolo and Gibilaro adequately estimates the onset of bubbling for both powders at all P , provided that experimentally determined values of n and u ′ t , are applied. For the d p = 112 μm powder, the theory of Foscolo and Gibilaro is applicable with calculated values of u t and experimental values of n .
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Fluid Flow Through Packed Columns
Şule Ergün · Medical Entomology and Zoology · 1952 · 7K citations
L.G. Leal · International Journal of Multiphase Flow · 1979 · 5.3K citations
D. Geldart · Powder Technology · 1973 · 3.4K citations
D. Geldart · Medical Entomology and Zoology · 1986 · 874 citations
Process Intensification, Chemical Engineering, Engineering +14