Summary
A simple unidirectional diffusion model is employed to analyze the axial dispersion of solid particles flowing through a rotary solid flow system, namely a rotary dryer. It is shown that the reciprocal of the Peclet number D/uL is uniquely correlated as a function of the dimensionless number F/dSN which characterizes the operating conditions of the rotary dryer.
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Abbreviations
- C :
-
concentration of tracer, mass/(length)3
- d :
-
diameter of rotary dryer, length
- d p :
-
diameter of solid particles, length
- D :
-
longitudinal dispersion coefficient or axial mixing coefficient, (length)2/time
- F :
-
volumetric flow rate of solid, (length)3/(length)2 time
- L :
-
length of rotary dryer, length
- N :
-
rate of rotations of dryer, time−1
- Q :
-
volume of tracer injected, based on bulk density of particles, (length)3
- S :
-
slope of the rotary dryer
- u :
-
average flow velocity, based on effective flow volume of dryer, length/time
- v :
-
volumetric flow rate, based on bulk density of particles, (length)3/time
- V :
-
effective volume of rotary dryer, (length)3
- x :
-
distance from entrance of experimental section of dryer, length
- θ :
-
time, measured from instant of introducing tracer into flowing material
- 1−ε :
-
volumetric solid hold-up fraction
- σ :
-
standard deviation
- σ 2 :
-
variance
- σ r :
-
relative standard deviation
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Fan, LT., Ahn, YK. Axial dispersion of solids in rotary solid flow systems. Appl. sci. Res. 10, 465 (1961). https://doi.org/10.1007/BF00411939
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DOI: https://doi.org/10.1007/BF00411939