In rotary dryer design and operation, what typical fraction of the drum volume is occupied by the solid hold-up (material actually resident inside the rotating shell during steady operation)?

Difficulty: Easy

Correct Answer: 0.05 to 0.15

Explanation:


Introduction / Context:
Rotary dryers are widely used in chemical and process industries to reduce moisture in granular, crystalline, or lumpy solids. A key operating parameter is the solid hold-up, meaning the fraction of the dryer shell volume that is actually occupied by solids at any moment under steady operation. Correctly estimating hold-up helps size the dryer, set residence time, and predict gas–solid contacting efficiency.



Given Data / Assumptions:

  • Cocurrent or countercurrent direct-fired rotary dryer handling free-flowing solids.
  • Flight (lifter) arrangement is typical for industrial units.
  • Operation is steady with normal fill levels—not start-up or emergency conditions.


Concept / Approach:
Inside a rotary dryer, solids are lifted and showered through the hot gas stream. Only a relatively small fraction of the cylinder cross-section is filled because excessive fill would suppress cascading and curtain formation, hurt heat/mass transfer, and increase power draw. Industry practice and pilot data typically show hold-up values in the low percentage range of total shell volume.



Step-by-Step Solution:

Define solid hold-up H as volume of solids inside the shell divided by the internal shell volume.For flighted rotary dryers with proper speed and slope, H is intentionally kept low to sustain good showering and cascade.Empirical ranges from design practice indicate H ≈ 0.05–0.15 (i.e., 5–15% of shell volume) for free-flowing solids at typical throughputs.


Verification / Alternative check:
Mass balance on solids (throughput = hold-up / residence time) combined with measured residence times in test units yields hold-up values generally in this 0.05–0.15 range for most granular products. Higher values are exceptional and can indicate suboptimal lifter design or sluggish materials.



Why Other Options Are Wrong:

  • 0.25 to 0.50: Too high; would impair falling curtain formation and cause excessive power consumption.
  • 0.50 to 0.80 and 0.80 to 0.90: Unrealistically high for rotary dryers; these fills are more like rotating kilns with bed flow, not efficient dryers.


Common Pitfalls:
Confusing mass hold-up with volumetric hold-up; ignoring the effect of flight design and rotational speed; assuming sticky or highly cohesive solids behave like free-flowing materials.



Final Answer:
0.05 to 0.15

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